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  • AUGUST 2014

    VOL. 53, NO. 8IN THIS ISSUE

    CORROSION PREVENTION AND CONTROL WORLDWIDE MATERIALS PERFORMANCE

    A 36-in (914-mm) diameter natural gas pipeline was recently recoated in the feld with an airless-spray two-part epoxy coating for protection against external corrosion. In October 2013, NACE International released an updated version of NACE SP0169, which addresses control of external corrosion on underground or submerged metallic piping systems. See the feature article beginning on page 24. Photo courtesy of Mears Group, Inc.

    MATERIALS SELECTION & DESIGN

    56An Analysis of the Updated Cost of Corrosion in IndiaR. Bhaskaran, Lalit Bhalla, Afzalur Rahman, Suruchi Juneja, Upma Sonik, Sukhpreet Kaur, Jasneet Kaur, and N.S. Rengaswamy

    66Welding Consumable Issues on Corrosion of X65QT SteelBalraj Velu, Rajnish Garg, Mukesh Saxena, and Paul Rostron

    72MSD Blog

    CATHODIC PROTECTION

    30CP Blog

    SPECIAL FEATURES

    24Updating NACE SP0169 for Controlling External Corrosion on Underground or Submerged Metallic Piping Systems Kathy Riggs Larsen

    76Pipes and Pipelines Supplier Guide

    COATINGS & LININGS

    32Power Plant Condenser Tube Sheet Retroft with Epoxy Cladding and CP EvaluationZhiyuan Liu and John Yang

    38CL Blog

    CHEMICAL TREATMENT

    46The Pursuit of a Green Carbon Steel Corrosion Inhibitor Part 1Matthew LaBrosse and Donovan Erickson

    50CT Blog

    About the Cover

    2 AUGUST 2014 MATERIALS PERFORMANCE NACE INTERNATIONAL: VOL. 53, NO. 8NACE INTERNATIONAL: VOL. 53, NO. 8

    24 66

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  • AUGUST 2014

    VOL. 53, NO. 8IN THIS ISSUE

    CORROSION PREVENTION AND CONTROL WORLDWIDE MATERIALS PERFORMANCE

    DEPARTMENTS

    6Up Front

    8The MP Blog

    14Material Matters 14. 3D scanning tool uses structured light to create images of pipe surface corrosion 18. Permanently installed guided wave testing tool facilitates frequent pipeline monitoring 21. Company News

    22Product Showcase

    96Spotlight on NACE International Corporate Members

    98I AM NACE

    111Building Business Connections 111. Corrosion Engineering Directory 115. Advertisers Index

    116Corrosion Basics

    116. Stress Corrosion Cracking

    NACE NEWS

    100NACE Area & Section News

    103New and Revised Standards Announced

    104NACE Foundation and Mears Group Team to Award Scholarship

    105NACE Corporate Members

    106Calendar of Events

    107 NACE Course Schedule

    109NACE Headquarters Directory

    MP (Materials Performance) is published monthly by NACE International

    (ISSN 0094-1492; USPS No. 333-860). Mailing address and Editorial

    Offces: 1440 South Creek Drive, Houston, TX 77084-4906; phone: +1

    281-228-6200. Internet address: www.nace.org. Preferred periodicals

    nonproft postage paid at Houston, TX and additional mailing offces.

    Canada Post: Publications Mail Agreement #40612608. Canada Returns

    to be sent to Pitney Bowes, PO Box 25542, London, ON N6C 6B2. Copyright

    2014 by NACE International. Reproduction of the contents, either as a whole

    or in part, is forbidden unless permission has been obtained from the

    publisher. Articles and editorials herein represent the opinions of the authors

    and not necessarily those of NACE. Advertising is included as an educational

    service, and products and/or services mentioned carry no implied or real

    endorsement or recommendation from NACE. NACE reserves the right to

    prohibit any advertisement that is not consistent with the objectives of

    NACE.

    POSTMASTER: Forwarding charges guaranteed. Send address changes to

    NACE FirstService, 1440 South Creek Drive, Houston, TX 77084-4906.

    SUBSCRIPTION RATES: To members as part of annual dues $12; U.S.

    nonmembers $115; overseas nonmembers $130; libraries $205; overseas

    libraries $220; single copy $20, availability permitting. Rates to nonmem-

    bers subject to change. Subscriptions must be prepaid. Claims made within

    6 months of issue date flled at no charge, availability permitting. Non-

    airmail overseas subscribers must wait 60 days from issue date to claim

    a replacement issue. Individual back issues may be available for up to 2

    years. Requests for address changes should include previous address of

    subscriber. Change of address should be provided 6 weeks prior to ensure

    continued delivery (phone: 1 800-797-6223 U.S. and Canada or +1 281-

    228-6223 worldwide or e-mail: [email protected]). Cancellation must

    be made in writing. Refunds will be prorated less a $20 processing fee.

    Information on becoming a NACE member can be obtained from the NACE

    Membership Services Department at the above phone number and e-mail

    address. PRINTED IN THE U.S.A.

    4 AUGUST 2014 MATERIALS PERFORMANCE NACE INTERNATIONAL: VOL. 53, NO. 8

    MP (Materials Performance) is published monthly by NACE International

    (ISSN 0094-1492; USPS No. 333-860). Mailing address and Editorial

    Offces: 15835 Park Ten Place, Houston, TX 77084; phone: +1 281-228-

    6200. Internet address: www.nace.org. Preferred periodicals nonproft

    postage paid at Houston, TX and additional mailing offces. Canada Post:

    Publications Mail Agreement #40612608. Canada Returns to be sent to

    Pitney Bowes, PO Box 25542, London, ON N6C 6B2. Copyright 2014 by

    NACE International. Reproduction of the contents, either as a whole or in

    part, is forbidden unless permission has been obtained from the publisher.

    Articles and editorials herein represent the opinions of the authors and not

    necessarily those of NACE. Advertising is included as an educational service,

    and products and/or services mentioned carry no implied or real endorse-

    ment or recommendation from NACE. NACE reserves the right to prohibit

    any advertisement that is not consistent with the objectives of NACE.

    POSTMASTER: Forwarding charges guaranteed. Send address changes to

    NACE FirstService, 15835 Park Ten Place, Houston, TX 77084. SUB-

    SCRIPTION RATES: To members as part of annual dues $12; U.S. nonmem-

    bers $115; overseas nonmembers $130; libraries $205; overseas libraries

    $220; single copy $20, availability permitting. Rates to nonmembers

    subject to change. Subscriptions must be prepaid. Claims made within

    6 months of issue date flled at no charge, availability permitting. Non-

    airmail overseas subscribers must wait 60 days from issue date to claim

    a replacement issue. Individual back issues may be available for up to

    2 years. Requests for address changes should include previous address of

    subscriber. Change of address should be provided 6 weeks prior to ensure

    continued delivery (phone: 1 800-797-6223 U.S. and Canada or

    +1 281-228-6223 worldwide or e-mail: [email protected]). Cancel-

    lation must be made in writing. Refunds will be prorated less a $20 process-

    ing fee. Information on becoming a NACE member can be obtained from

    the NACE Membership Services Department at the above phone number

    and e-mail address. PRINTED IN THE U.S.A.

    14 18

    104

    HELP. NEED PHOTO

    6

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  • Kathy Riggs Larsen

    6 AUGUST 2014 MATERIALS PERFORMANCE NACE INTERNATIONAL: VOL. 53, NO. 8

    Pipeline Coating Assessment Facility Opens in Australia The National Facility for Pipelines Coat-

    ing Assessment, an initiative of the Energy

    Pipeline Co-operative Research Centre

    (CRC), was recently launched at Deakin

    Universitys Waurn Ponds campus in Vic-

    toria, Australia and will be jointly man-

    aged by the universitys School of Engi-

    neering and Institute for Frontier

    Materials. The independent facility will

    perform coating testing for oil and gas

    pipelines and provide research that sup-

    ports pipeline coating selection and devel-

    opment. The Energy Pipelines CRC is a

    collaboration between Deakin, the Uni-

    versity of Wollongong, Adelaide Univer-

    sity, the Australian National University,

    and the Australian Pipeline Industry As-

    sociation. Source: Deakin University,

    www.deakin.edu.au.

    Spray-Applied Composite Protects Metals from Corrosion

    Photo by Uwe Bellhuser.

    An environmentally friendly spray-

    applied composite material developed by

    material researchers at the INMLeibniz

    Institute for New Materials (Saarbrcken,

    Germany) prevents corrosion of metals

    exposed to aggressive aqueous solutions,

    including salt solutions such as seawater

    and salt spray on roads and aqueous acids

    like acid rain. This is accomplished by the

    protective layers structure, which is a few

    micrometers thick. Several layers of pro-

    tective particles are placed on top of each

    other in an offset arrangement (similar to

    roof shingles) to form a self-organized,

    highly structured barrier. The composite,

    which can be used to coat plates, pipes,

    gear wheels, tools, machine parts, etc., ad-

    heres to the metal substrate after thermal

    curing at 150 to 200 C, and is suitable for

    steels, aluminum, magnesium, copper,

    and metal alloys. For more information,

    visit www.inm-gmbh.de.

    Monitoring Sewer Gases Can Determine Corrosion RiskResearchers with the University of Colo-

    rado Boulder report that certain condi-

    tions in wastewater pipes can help utili-

    ties determine which ones need repairs.

    Microbe communities have long been rec-

    ognized as a factor in concrete pipe corro-

    sion, but they have not been well studied.

    To fill in the gaps, the research team mea-

    sured bacterial diversity, gas concentra-

    tions in the air above the waste water, and

    other factors from 10 different sewer sys-

    tems in major U.S. cities. In the most worn

    pipes, they observed elevated levels of

    both hydrogen sulfide (H2S) and carbon

    dioxide (CO2) gases as well as low diversity

    in the types of bacteria present. The re-

    searchers concluded that wastewater util-

    ities could economically monitor combi-

    nations of these gases in sewage pipes to

    determine which sites might be at higher

    risk for corrosion. Source: American

    Chemical Society, www.acs.org.

    Self-Protecting Coatings Contain Inhibitors to Prevent Corrosion A team of researchers from Max Plank

    Institute of Colloids and Interfaces (Pots-

    dam, Germany) explored how self-protect-

    ing anticorrosion coatings that contain

    embedded spherical nanocontainers filled

    with a corrosion inhibitor can be used to

    autonomously protect expensive and

    often difficult-to-reach metal parts and

    infrastructure from surface corrosion.

    Most conventional coatings are thinner

    than 100 m, so nanocontainers should be

    at least three times smaller in size to be

    properly integrated into the coating. How-

    ever, the total amount of a crack sealant

    that can be loaded into these containers

    isnt adequate to completely fill a typical

    submillimeter-size scratch in the coating.

    To overcome this problem, the researchers

    extended the approach by using corrosion

    inhibitors as the nanocontainers load. In

    this situation, theres no need to cover the

    scratch completelythe inhibitor ad-

    sorbed onto the scratchs bare metal sur-

    face can safely mitigate further corrosion

    development. To read more, see the

    Corrosion paper at http://dx.doi.org/

    10.5006/0976.

    Warning System Uses Coating to Detect Cracks in Concrete

    Sensing skin report. Image by Aku

    Seppnen.

    A new sensing skin technology devel-

    oped by researchers from North Carolina

    State University (Raleigh, North Carolina)

    and the University of Eastern Finland is

    designed to serve as an early warning sys-

    tem for concrete structures, allowing au-

    thorities to respond quickly to damage in

    critical infrastructure. The skin is an elec-

    trically conductive coating that can be ap-

    plied to new or existing structures. Elec-

    trodes are applied around the perimeter of

    a structure, and the sensing skin is

    painted onto the structure and over the

    electrodes. A computer program then runs

    a small current between two of the elec-

    trodes at a time, cycling through a number

    of possible electrode combinations. Every

    time the current runs between two elec-

    trodes, a computer monitors and records

    the electrical potential at all of the elec-

    trodes on the structure. If the skins con-

    ductivity decreases, that means the struc-

    ture is cracked or damaged. A suite of

    algorithms registers damage and deter-

    mines where the damage has taken place.

    To learn more, visit news.ncsu.edu.

    UP FRONT

    August 2014 MP.indd 6 7/21/14 7:40 AM

    http://www.deakin.edu.auhttp://www.inm-gmbh.dehttp://www.acs.orghttp://news.ncsu.eduhttp://dx.doi.org/10.5006/0976http://dx.doi.org/10.5006/0976

  • August 2014 MP.indd 7 7/21/14 7:42 AM

    mailto:[email protected]://www.elcometer.commailto:[email protected]://www.elcometer.com

  • Editor:In the May 2014 issue of MP there were

    two excellent articles on corrosion and materials for carbon capture and seques-tration (CCS). Although corrosion is certainly a consideration when liquid water is present, it is not when water is soluble in supercritical CO

    2 (SC-CO

    2) and

    no free water phase is present. However, for transport of SC-CO

    2 to the location of

    injection for CCS, the most common material for pipelines is carbon steel, which has been the mainstay of the oil and gas industry for over 30 years for enhanced oil recovery (EOR). Yet while corrosion is not an issue, the most impor-tant design consideration for transport of SC-CO

    2 is the risk of a long-running

    ductile fracture. This requires modeling of the decompression behavior of the CO

    2

    being transported coupled with the so-called Battelle two curve method. There are numerous references and sources on this design requirement; however, I felt the readers should be made aware, since this is Materials Performance, and not just a corrosion publication, that even after corrosion is considered for SC-CO

    2 there are still

    major materials properties that must also be evaluated for CCS.

    Bruce Craig, Subject Matter Expert, Materials and Corrosion, Stress Engineering

    Services, Inc., Houston, Texas, USA

    The following are excerpts from the NACE

    International Corrosion Network (NCN)

    and NACE Coatings Network. These are

    e-mail-based discussion groups for corro-

    sion professionals, with more than 3,000

    participants.

    The excerpts are selected for their

    potential interest to a large number

    of NACE members. They are edited for

    clarity and length. Authors are kept

    anonymous for publication.

    Please be advised that the items are

    not peer-reviewed, and opinions and

    suggestions are entirely those of the

    inquirers and respondents. NACE does

    not guarantee the accuracy of the techni-

    cal solutions discussed. MP welcomes

    additional responses to these items. They

    may be edited for clarity.

    For information on how to subscribe

    to these free list servers, click on the

    Corrosion Central link and then Online

    Corrosion Community List Servers on the

    NACE Web site: www.nace.org.

    Weld degradation from muriatic acid

    Q: Heavy-duty equipment, such as concrete skips and system

    propping, is often returned to us heavily encrusted with dried concrete or cement, so they are regularly soaked/cleaned with a variety of powerful concrete removers/cleaners normally used for cleaning brickwork, tiles, etc.

    On average, these cleaners contain between 12 and 18% muriatic (hydrochlo-ric) acid (HCl) and 1 to 6% sulfuric acid (H

    2SO

    4), both of which we know to be

    highly corrosive to metals.The equipment in question is

    commonly sprayed or brushed with copious amounts of these cleaners and often allowed to soak overnight (sometimes much longer) before being hosed or washed down.

    A concrete skip can carry up to 5.5 metric tons of material, which is then hauled by crane to tremendous heights and may even be suspended for lengthy periods of time on a bridle supported only by two swivel pins.

    Can the long-term, continuous use of these corrosive chemicals allow them to penetrate and damage the equipments structural or load-bearing welds?

    Having seen numerous photos showing the corrosive effects of these chemicals on various types of metal plate, and knowing that the same acids are used to clean metal in the production of stain-less steel, you can understand my concern when considering that the weld is gener-ally the weakest point of any equipment. Many of these concrete skips are now several years old (some more than 10) and over this period, a variety of these chemi-cal cleaners have been used with much gusto.

    Are my concerns warranted and am I worrying about nothing? Is there a research paper or any other reference or scientific document that I may obtain/purchase that covers the above issues?

    THE BLOG

    Continued on page 10

    EDITORIAL

    DIRECTOR, CONTENT DEVELOPMENT/ Gretchen A. Jacobson

    MANAGING EDITOR

    TECHNICAL EDITOR John H. Fitzgerald III, FNACE

    ASSOCIATE EDITOR Kathy Riggs Larsen

    EDITORIAL ASSISTANT Suzanne Moreno

    CONTRIBUTOR Husna Miskinyar

    GRAPHICS

    ELECTRONIC PUBLISHING Teri J. Gilley

    COORDINATOR

    GRAPHICS DESIGNER Michele S. Jennings

    ADMINISTRATION

    CHIEF EXECUTIVE OFFICER Robert (Bob) H. Chalker

    GROUP PUBLISHER William (Bill) Wageneck

    ADVERTISING

    SALES MANAGER Diane Gross

    [email protected],

    +1 281-228-6446

    ASSISTANT SALES MANAGER Teresa Wright

    [email protected],

    +1 281-228-6472

    ACCOUNT EXECUTIVES Erica R. Cortina

    [email protected],

    +1 281-228-6473

    Brian Daley

    [email protected],

    +1 281-228-6455

    Pam Golias

    [email protected],

    +1 281-228-6456

    Jody Lovsness

    [email protected],

    +1 281-228-6257

    Leslie Whiteman

    [email protected],

    +1 281-228-6248

    ADVERTISING/BOOKS Brenda Nitz

    COORDINATOR [email protected],

    +1 281-228-6219

    REGIONAL ADVERTISING SALES The Kingwill Co.

    REPRESENTATIVES Chicago/Cleveland/

    New York Area

    [email protected],

    +1 847-537-9196

    NACE International Contact Information

    Tel: +1 281-228-6200 Fax: +1 281-228-6300

    E-mail: [email protected] Web site: www.nace.org

    EDITORIAL ADVISORY BOARD

    John P. Broomfield, FNACE Broomfield Consultants

    Raul A. Castillo Consultant

    Irvin Cotton Arthur Freedman Associates, Inc.

    Arthur J. Freedman Arthur Freedman Associates, Inc.

    David D. He PG&E

    Orin Hollander Holland Technologies

    W. Brian Holtsbaum Corsult Associates (1980), Ltd.

    Russ Kane iCorrosion, LLC

    Ernest Klechka CITGO Petroleum Corp.

    Kurt Lawson Mears Group, Inc.

    Lee Machemer Jonas, Inc.

    Norman J. Moriber Mears Group, Inc.

    John S. Smart III John Smart Consulting Engineer

    L.D. Lou Vincent L.D. Lou Vincent PhD LLC

    8 AUGUST 2014 MATERIALS PERFORMANCE NACE INTERNATIONAL: VOL. 53, NO. 8

    August 2014 MP.indd 8 7/21/14 7:42 AM

    http://www.nace.orgmailto:[email protected]:[email protected]:[email protected]:[email protected]:[email protected]:[email protected]:[email protected]:[email protected]:[email protected]:[email protected]://www.nace.org

  • August 2014 MP.indd 9 7/21/14 7:42 AM

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  • A: Te short answer is yes, your concerns are warranted. Any

    crevices will be subject to accelerated corrosion. I would be doubtful welds are perfect 100% of the time.

    A: A more serious concern could be the evolution of nascent hydrogen

    by acids, which could be absorbed by the steel or weld material and cause cracking. I have seen cracking on scafolding clips that we attributed to hydrogen absorp-

    tion and cracking due to improper acid cleaning techniques.

    Cracking of the base material would only be a problem for higher-strength steels, and skip base material would not, I would think, be at risk. However, depend-ing upon the welding procedure followed, the welds could be at risk. The swivel pins, if exposed to the acid, could be of particular concern.

    I think it would be worthwhile having a few welds, pad eyes, and swivel pins destructively analyzed for cracking to see if there is a problem before you have a failure in the field.

    A: We know from many sources that hydrogen generated from acid

    attack will cause fracture of hardened steels. Te difcult part is to establish how severe the attack must be before the materials in your equipment are compro-mised. If they are all mild steel, the most you should expect is an occasional blister. On the other hand, if there are hardened components, there is a good probability of occasional failures. It sounds like you are firting with disaster and, in addition, it seems it would be very difcult to accurately duplicate the type of feld conditions you describe in a laboratory environment. On the other hand, there are probably thousands of similar cement truck applications around the world and we havent heard of many drums rolling loose.

    Condenser materials

    Q: I am looking at a steam surface condenser that may use circulat-

    ing water with a chloride concentration of up to 7,000 mg/L. What materials can be used for the condenser tubes/tubesheets, etc.? I understand that most stainless steels (SS) cannot withstand this level of chlorides. Is there a way to predict the life of those tubes under those conditions?

    A: Te best tube material is titanium. Several SS and copper

    alloys are also okay. For utility applica-tions, however, copper may cause problems in the turbine.

    A: We have titanium condenser tubes and a Muntz metal

    tubesheet, and have had to coat the tubesheet to prevent leaks. Titanium does not easily roll in, and the tubesheet undergoes galvanic corrosion at the tube

    BLOG

    Continued from page 8

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  • interface. Use of dissimilar metals should be avoided!

    A: I agree that titanium would be a good choice, but would the

    copper-based alloys be the most suitable materials in terms of their performance and cost? Many of the steam surface condensers work well with 90-10 Ci-Ni or 70-30 Cu-Ni tubes where the cooling medium may be seawater.

    A: In my country, we use copper-based alloys, especially 70-30

    Cu-Ni, and we have had very good results. The chloride concentration of circulating water is nearly 19,000 mg/L. Titanium is a good choice, but is expensive and you have to consider the galvanic corrosion.

    A: Copper-based alloys with due regard for water quality have

    been successfully used for many years in seawater heat exchanger applications. They can offer benefits over SS in terms of crevice corrosion behavior and recovery from upset.

    A: When using titanium materials, use caution if cathodic protection

    is used to control galvanic corrosion. The very noble potential of titanium can only be brought to 0.650 off vs. a copper/copper sulfate (Cu/CuSO

    4) reference

    electrode without danger of hydrogen embrittlement. This danger would certainly eixist with magnesium and possibly even with zinc condenser anodes during times of no water f low. One should consider the old-school wisdom: Avoid use of dissimilar metals.

    A: Te present slowing of deliveries of titanium are making people

    reexamine alternative materials such as super ferritic and super-austenitic SS and Cu-Ni for seawater-cooled heat exchang-ers and condensers. Regarding Cu-Ni, 90-10 has been favored by the U.S. Navy since it was frst introduced in 1950, the main reason being that 90-10 has suf-cient fouling resistance in seawater to eliminate the need for chlorination. Unfortunately, 90-10 has to be periodi-cally replaced since it sufers from poor resistance to erosion-corrosion and very much accelerated corrosion in the presence of traces of hydrogen sulfde (H

    2S) (e.g., 3 ppm), and gives rise to the

    turbine problems in certain applications. As of a couple of years ago, the U.S. Navy

    Continued on page 12

    Copper-based alloys with due regard for water quality

    have been successfully used for many years in seawater

    heat exchanger applications.

    11NACE INTERNATIONAL: VOL. 53, NO. 8 MATERIALS PERFORMANCE AUGUST 2014

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  • was focused on using titanium shipboard condensers together with specifc chlori-nation and dechlorination procedures. I would therefore examine and weigh the materials choices very carefully.

    A: From my experience, people need to be extremely cautious about

    mixing Cu-Ni and SS in seawater systems where Cu-Ni piping has failed locally in the vicinity of SS fttings, and also where Cu-Ni tubes have failed where attached to a SS tubesheet. It is not obvious from looking at a galvanic series in seawater that Cu-Ni and SS are incompatible. Use either all SS or all copper-based materi-als, and never mix the two!

    Caustic embrittlement

    in reinforced concrete

    Q: Are there documented cases of caustic embrittlement of

    reinforcing steel in concrete? When I look

    at the Pourbaix diagram for water and Fe, I am tempted to say that under certain conditions of potential, although the pH is caustic, you will get embrittlement.

    A: I have never heard of this occur-ring. Also, I have never heard of

    caustic embrittlement of steel at normal ambient temperatures, where concrete is generally used. At elevated temperatures, the Pourbaix diagram is altered by expan-sion of the domain of stability for dissolved species. Te application of a cathodic current in an environment that contains calcium ions could lead to the formation of protective calcareous deposits.

    A: Ive never heard of it in concrete. Tere can be hydrogen embrittle-

    ment with excessive cathodic protection applied to high-strength steels used for prestressing. High alkali content in the cement can attack some siliceous aggre-

    gate and rocks used in concrete through a process known as alkali silica reaction, but that is not a metal thing.

    The alkalinity of concrete comes from the cement. When water is added to the mix, the cement rapidly produces a saturated lime (calcium hydroxide [Ca(OH)

    2]) solution that has a nominal pH

    of about 12.6. In the cement there are also alkali oxides present including sodium oxide (NaO) and potassium oxide (KO), which react with the mix water to produce sodium hydroxide (NaOH) and potassium hydroxide (KOH). These alkali hydroxides typically push the pH of concrete up to and past pH 13. In the ASM Handbook, Vol. 13C, Corrosion: Environments and Industries (2006), in the chapter on Corrosion in Bridges and Highways, the role of pore water pH and chloride-initiated corrosion is discussed. It reports that a concrete with a pH of 13.6

    BLOG

    Continued from page 11

    12 AUGUST 2014 MATERIALS PERFORMANCE NACE INTERNATIONAL: VOL. 53, NO. 8

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  • has a chloride content corrosion thresh-old about five times that of a lower alkali content concrete with a pH of 13.2.

    The pH of cements used in Europe and concretes made in North America with pozzolans like f ly ash and silica fume is lower than standard mixes made with Type I/II cements. This is because slag cements are often used in Europe, and because pozzolans react with Ca(OH)

    2

    and the pH is reduced. Given the number of structures that have been built with non-pozzolan Type I/II cements, if caustic embrittlement were a problem, the cement alkali content would long ago have been restricted.

    Use of silver

    Q: How does silver perform in corrosive environments? In the

    past it has been assumed that silver is very noble and therefore has been used for downhole and other hydrogen sulfide (H

    2S) service conditions.

    A: In addition to being very expen-sive in comparison with struc-

    tural metallic materials, silver has a strong afnity for sulfur with which it forms a nonprotective surface compound. Te ASM Metals Handbook notes that even indoor atmospheres in large cities that contain traces of sulfur compounds cause sulfdation of silver at a rate in the order of 70 micrograms per dm2 per day. Te handbook also notes that surface plating of silver by rhodium over a nickel under-plate prevents tarnishing.

    A: Principle applications of silver are in electronic contacts and

    circuit boards. Such applications are discussed in the Instrument Society of America Standard ISA S71.04 published in 1985 (which sets limits for contami-nants found in the environment) and various other publications. See NACE International CORROSION 2007 paper no. 07400, for example, which principally concerns copper components but also references corrosion data for silver.

    A: Tere are many old texts describ-ing the corrosion behavior of

    silver, including the 8th edition of the ASM Metals Handbook, Vol. 1, pp. 1,181-1,185.

    Editors Note: Additional MP Blog items appear in the individual technical sections:

    cathodic & anodic protection (p. 30), coatings & linings

    (p. 38), chemical treatment (p. 50), and materials selection & design (p. 72).

    13NACE INTERNATIONAL: VOL. 53, NO. 8 MATERIALS PERFORMANCE AUGUST 2014

    August 2014 MP.indd 13 7/21/14 7:42 AM

    http://www.corrpro.comhttp://www.corrpro.com

  • MATERIAL MATTERS

    3D scanning tool uses structured light to create images of pipe surface corrosion

    To successfully evaluate features

    that may impact a pipeline or

    other structures fitness for ser-

    vice, field data are collected on

    corrosion defects in hazardous liquid and

    gas pipelines after inline inspection runs,

    direct assessment, and other mainte-

    nance activities. These data may need to

    be further assessed using quantitative

    also known as phase measurement pro-

    filometry (PMP), to acquire 3D data. This

    technique uses projected light patterns

    and a camera to create a 3D image of the

    surface under inspection, and an analyti-

    cal software program that enables analy-

    sis of the 3D data. The measurement

    approach used by the tool falls into a

    class of 3D measurements called triangu-

    lation. Our eyes ability to assess three

    dimensions is, for most people, based on

    triangulation, says Matt Bellis, president

    of Seikowave. A camera takes the place of

    one eye and a projector is a substitute for

    the other eye. Triangles are formed

    between the camera sensor, the projector,

    and the object under inspection.

    To take a measurement of an object,

    Bellis explains, specific patterns that

    vary over time are projected onto the

    object, and the camera captures images

    of the object illuminated by the patterns

    and computes the 3D pointscollecting

    300,000 voxels (volumetric pixels or 3D

    pixels) per scan. Based on the varying

    projected patterns, a very precise triangle

    is formed between the camera and the

    object, which makes it possible to capture

    the 3D features of the surface with a level

    of precision within several thousandths of

    an inch. Once the data are acquired, the

    software generates a 3D image that repli-

    cates the objects surface. With this tech-

    nology, the features of a pipes surface

    topography can be accurately measured

    within 2 mils (51 m), says Joseph Pikas,

    vice president of pipeline integrity with

    Technical Toolboxes.

    The 3D structured light tool is typi-

    cally used when the results of an inline

    inspection, such as an intelligent pig run,

    indicate an anomaly on an area of the

    tools to determine key parameters such

    as the maximum allowable operating

    pressure (MAOP) of the pipeline. Accu-

    rately calculating the severity of defects

    such as corrosion pitting, dents, and

    gouges helps determine the remaining

    strength of the structure and whether or

    not repair or replacement is required.

    Technical Toolboxes (Houston, Texas)

    and Seikowave, Inc. (Lexington, Ken-

    tucky) have developed and ruggedized a

    field tool, the 3D Toolbox, that measures

    the surface of any type of metallic pipe or

    structure and creates a three-dimen-

    sional (3D) model of the surface. The tool

    comprises a 3D imaging system that uti-

    lizes the 3D structured light technique,

    A technician uses the 3D structured light scanning tool to take scans of external corrosion on a pipe

    in the Algerian Desert. Photo courtesy of Joseph Pikas.

    14 AUGUST 2014 MATERIALS PERFORMANCE NACE INTERNATIONAL: VOL. 53, NO. 8

    August 2014 MP.indd 14 7/21/14 7:42 AM

  • pipe and an additional inspection is nec-

    essary to verify the severity of the anom-

    aly. Most types of anomalies that can be

    observed visually can be assessed with

    the 3D structured light scanning tool.

    These include corrosion, gouges, and

    dents. Taking a 3D image is similar to

    capturing an image with a two-dimen-

    sional camera. The camera is aimed at the

    anomaly to be inspected and the mea-

    surement is captured and stored digitally

    on the laptop computer that is part of the

    system. It takes less than one second to

    acquire a 3D image.

    The procedure for examining the pipe

    with the 3D structured light scanning

    tool is similar to the procedure used when

    examining a pipe manually with a con-

    ventional pit gauge. Before taking a scan,

    Continued on page 16

    the pipe surface must be cleaned to

    remove old coatings and debris, and pre-

    pared to white metal1 or near white

    metal2 by abrasive blasting or another

    approved method to remove corrosion

    products and scale. Drawing a grid on the

    pipe to mark points for gauge readings is

    not necessary.

    In the case of a corrosion anomaly, the

    software processes the 3D images and

    creates a 3D model of the pipe surface

    that is used to determine the maximum

    pit depth of the corroded area. Once the

    operator selects the grid size and interac-

    tion rules for pitting, the software plots

    the river bottom profile, which indicates

    the deepest defects and their location in

    the corroded area of the pipe surface. The

    data can be used to calculate the MAOP

    Currently the 3D scanning tool is being tested for submarine and offshore applications. Photo

    courtesy of Seikowave.

    15NACE INTERNATIONAL: VOL. 53, NO. 8 MATERIALS PERFORMANCE AUGUST 2014

    Information on corrosion control and prevention

    August 2014 MP.indd 15 7/21/14 7:42 AM

    http://www.FarwestCorrosion.comhttp://www.FarwestCorrosion.com

  • Continued from page 15

    Left: A 3D image generated from a scan of a segment of corroded pipe with an original wall thickness of 0.5 in (13 mm). Right: A corrosion analysis of

    the corroded pipe. The 3D river bottom profle is shown in the upper right photo, and a graph of the corrosion profle is shown beneath it. Images

    courtesy of Joseph Pikas.

    16 AUGUST 2014 MATERIALS PERFORMANCE NACE INTERNATIONAL: VOL. 53, NO. 8

    MATERIAL MATTERS

    August 2014 MP.indd 16 7/21/14 7:43 AM

    http://www.elcometer.commailto:[email protected]://www.elcometer.commailto:[email protected]

  • and the predicted burst pressure using

    RSTRENG (external pipeline corrosion

    evaluation software), ASME B31G,3 or

    Modified B31G. According to Bellis, the

    RSTRENG effective area calculation,

    which incorporates the river bottom pro-

    file, provides the most repeatable MAOP

    calculation.

    The 3D structured light technology is

    an easier and faster method to determine

    the river bottom profile than any manual

    assessment. In a manual assessment,

    technicians draw a grid on the pipeline

    and take depth measurements at inter-

    secting points with a pit gauge; this is a

    time-consuming process and is subject to

    human error, Pikas says. A recent exam-

    ple, he notes, was an 8-ft (2.4-m) length of

    pipe with corrosion completely along the

    bottom between the 4 oclock to 8 oclock

    positions on the pipes circumference.

    With a 0.5-in (13-mm) grid, it would

    require over 10,000 manual readings to

    determine the river bottom profile; this

    could take as long as a day and a half.

    With the 3D structured light scanning

    tool, the 3D images could be acquired in

    less than an hour. The software can ana-

    lyze the data and provide a river bottom

    profile, maximum safe operating pres-

    sure, and predicted burst pressure within

    a few minutes. Decisions can be made in

    the field regarding the type of action to

    take to address the anomalylower the

    operating pressure, repair the pipe with a

    composite sleeve, recoat the pipe, replace

    a section of pipe, etc.

    To ensure correct calculation of the

    burst pressureor failure pressureand

    safe pressure of the pipe, its very impor-

    tant that the depths along the river bot-

    tom are accurately measured, says Joe

    Summa, president of Technical Tool-

    boxes. Today were seeing river bottoms

    run almost to the extent of the entire

    length of the pipe joint: up to 40 ft (12 m).

    Additionally, Summa notes, determining

    the depth and location of the deepest

    points manually when the corrosion is

    complicated is challenging and it can be

    difficult for a technician to accurately

    gauge corrosion depths where a large por-

    tion of the pipe surface is corroded. This

    is especially true when there is a signifi-

    cant amount of pitting and little or no

    parent metal to which a manual pit gauge

    can be anchored.

    In a 3D analysis, the original condi-

    tion of the pipe is used as a baseline,

    Summa explains. Separate data are col-

    lected for both damaged and undamaged

    areas of the pipe. Once the undamaged

    points are identified, they are used to

    form surfaces that serve as a reference

    against which damaged areas are mea-

    sured. The extent of metal loss or defor-

    mation can then be determined, he says.

    Using the 3D structured light scan-

    ning tool, even when considering opera-

    tor and tool variability, the variation in

    predicted burst pressure is

  • The GWT tools transducer array is attached with adhesive to the pipe surface at a particular axial

    location, enclosed with a cover, and connected by cable to the pulser-receiver through a junction

    box interface. Photo courtesy of Plant Integrity, Ltd.

    18 AUGUST 2014 MATERIALS PERFORMANCE NACE INTERNATIONAL: VOL. 53, NO. 8

    MATERIAL MATTERS

    Permanently installed guided wave testing tool facilitates frequent pipeline monitoring

    To assist in detecting corrosion in oil and gas pipelines, Plant Integrity, Ltd. (Cambridge, United Kingdom), a subsid-

    iary of TWI, Ltd., has designed an ultra-

    sonic guided wave testing (GWT) tool for

    permanent installation. The tool, Teletest

    Permamount, uses low-frequency, long-

    range guided waves to monitor pipe walls

    for metal loss. The tool can identify

    areas where changes in the pipe wall

    cross-section thickness are occurring

    along the entire length of pipeline being

    monitored.

    According to Paul Jackson, general

    manager with Plant Integrity, this nonde-

    structive testing (NDT) technology was

    developed to cost-effectively enable

    repeated GWT and monitoring of pipe-

    lines that are difficult to access or in

    areas where the environment is hostile or

    safety may be an issue, such as buried or

    elevated pipelines, offshore risers, jetty

    lines, and pipelines that cross under

    roads or rivers. The permanent tool is

    intended to be used where traditional

    GWT can be successfully implemented. In

    many cases, Jackson says, the cost of

    accessing a pipeline far exceeds the cost

    of the NDT inspection. He uses a buried

    pipe as an example, where the costs to

    access a point on the pipe to conduct the

    test include excavating, shoring the

    trench, and backfilling the trench after-

    ward. To help reduce the costs for pipe

    access when the pipe needs to be tested

    multiple times, the permanent GWT tool

    is left in place on the pipe after it is

    installed and the testing process is man-

    aged from a more accessible location.

    In addition to delivering a more con-

    venient approach for repeatedly inspect-

    ing pipelines with GWT, the permanent

    tool also provides a means to increase

    the sensitivity of the inspection data,

    Jackson comments. The sensitivity of

    GWT is stated in terms of the minimum

    detectable percentage of change in a pipe

    walls cross-sectional area, and typically

    GWT inspections can identify cross-

    section loss of ~5 to 9%. Because the per-

    manently installed GWT tool facilitates

    more frequent testing, a baseline can be

    established. When current test data are

    compared to previous data, much smaller

    degrees of cross-section change within

    the pipe wall can be determineddown

    to 1%. The testing frequency, he adds, can

    be established based on the risk associ-

    ated with the pipe being monitored. Data

    can be collected more frequently for

    high-risk pipelines or for localized por-

    tions of a pipeline with a known problem

    area, and less frequently for low-risk

    pipelines.

    The tool is based on the GWT technol-

    ogy first developed by TWI in the 1990s to

    detect corrosion under insulation (CUI)

    in oil and gas pipelines. It uses the same

    basic components as traditional guided

    wave NDTa transducer ring (an array

    comprised of multiple transducers) that

    fits around the circumference of the pipe-

    line and generates low-frequency acoustic

    waves (usually

  • Continued on page 20

    The scan displays repeatable data from the tool. The responses in blue and green, grouped in

    terms of temperature, were taken weeks apart but show minimal comparable error when overlaid.

    The error can be quantifed by taking a residual between the two signals, which is displayed here as

    the red trace. Image courtesy of Plant Integrity, Ltd.

    19NACE INTERNATIONAL: VOL. 53, NO. 8 MATERIALS PERFORMANCE AUGUST 2014

    insulation doesnt need to be completely

    removed. The tool can be installed over

    protective coatings such as fusion-

    bonded epoxy and operate on pipes with

    diameters ranging from 2 to 48 in (51 to

    1,219 mm) and temperatures ranging

    from 40 to 80 C.

    The permanent transducer array will

    sit dormant until it is connected to a

    pulser-receiver, which directs the trans-

    ducer array to generate low-frequency

    acoustic waves that propagate in both

    directions along the pipeline. According

    to Jackson, the guided waves can propa-

    gate ~100 ft (30 m) in both directions from

    the transducer array and provide 100%

    pipe wall coverage. Pipe conditions can

    influence the wave range, he says. If the

    surface of the pipe wall is coated or

    degraded (e.g., with pitting corrosion) or

    the pipe geometry is complex, the dis-

    tance of the wave transmission may be

    reduced. Additionally, the wave distance

    is affected by the viscosity of the pipe con-

    tents and can be reduced as the contents

    viscosity increases. For a straight,

    aboveground bare metal pipe conveying

    gas, wave propagation distances of up to

    590 ft (180 m) in both directions have

    been achieved.

    Two symmetric wave modes are trans-

    mitted and received by the pulser-

    receiverlongitudinal waves, which are

    similar to compression waves, and tor-

    sional waves, which have more of a twist-

    ing motion. Jackson explains that where

    there is a change in the cross-sectional

    area of the pipe wall, such as a weld, bend,

    or defect caused by corrosion, these

    waves will convert into a f lexural wave.

    This change in acoustic impedance is

    ref lected back to the transducer array as

    an echo. The distance of the detected fea-

    ture from the transducer array can be

    determined using the speed of the initial

    wave and the receive time of the echo.

    The test data collected by the pulser-

    receiver can be probed in two ways. At the

    junction box, an operator can either col-

    lect and interpret the data in situ via a lap-

    top computer and the accompanying soft-

    ware program, or swap out the replaceable

    data storage component on the pulser-

    receiver unit and interpret the data at a

    different location. In remote locations, a

    battery-operated pulser-receiver can be

    connected to the transducer array at the

    junction box for several weeks to collect

    data in bursts, then be removed and

    Information on corrosion control and prevention

    August 2014 MP.indd 19 7/21/14 7:43 AM

    http://www.gmcelectrical.nethttp://www.gmcelectrical.net

  • Continued from page 19

    20 AUGUST 2014 MATERIALS PERFORMANCE NACE INTERNATIONAL: VOL. 53, NO. 8

    MATERIAL MATTERS

    reconnected at a later date to collect

    another burst of data. The software pro-

    gram interprets the data and presents

    them as A-scans, which display the ampli-

    tude of the reflected waves and their dis-

    tance from the transducer array, and

    C-scans, which plot the reflected ampli-

    tude using a color scale and show the fea-

    tures circumferential orientation as well

    as distance from the transducer array.

    Because welds are at known distances

    from the transducer array and have a typ-

    ical echo response, they are used to cali-

    brate the tool so areas of cross-section

    reduction can be located. To estimate the

    degree of cross-sectional change, a sys-

    tem of distance amplitude correction

    (DAC) curves is used. GWT is considered

    a screening method and currently there

    are no means of determining the dimen-

    sions of a detected f law. Typically, when

    remaining wall thickness measurements

    are required, a quantitative follow-up

    technique is used where metal loss is

    detected by GWT.

    Longevity and repeatability of data

    are critical for a permanently installed

    GWT tool, which must remain stable over

    long periods of time in harsh environ-

    ments. So that test results are repeatable

    and small changes in pipe condition can

    be detected, the coupling force between

    the transducers and the pipe is carefully

    controlled so variability with tempera-

    ture is minimal. This is done with a back-

    ing mass on the transducer, a controlled

    bond line between the transducer and the

    pipe, and an individual transducer pres-

    sure. During data collection, temperature

    is also monitored at the tool.

    So that components remain

    unchanged during the tools service life,

    which is designed to be five to 10 years, all

    components are fabricated to meet IP691

    ratings for protection against water

    immersion and dust ingress for subsea

    applications as well as pipelines that are

    buried.

    Contact Kamer Tuncbilek, Plant Integrity,

    Ltd.e-mail: kamer.tuncbilek@plantinteg-

    rity.co.uk.

    Reference1 BS EN 60529:1992+A2:2013, Degrees of protec-

    tion provided by enclosures (IP code) (Lon-

    don, U.K.: BSI, 1992).

    BibliographyJackson, P., Guided wave activity at TWI, http://

    youtu.be/Jhf5e7P515M ( June 17, 2014).

    K.R. Larsen

    August 2014 MP.indd 20 7/21/14 7:43 AM

    http://www.lidaproducts.comhttp://www.denora.comhttp://www.denora.commailto:[email protected]://www.lidaproducts.comhttp://www.denora.comhttp://www.denora.commailto:[email protected]:[email protected]:[email protected]://youtu.be/Jhf5e7P515Mhttp://youtu.be/Jhf5e7P515M

  • COMPANY NEWS

    OEL Products Acquires Ammonite and Cormetrics

    Jim ORourke, Presi-

    dent of OEL Proj-

    ects, Ltd., is pleased

    to announce the

    companys acquisi-

    tion of Ammonite

    Corrosion Engineer-

    ing and Cormetrics,

    Ltd. Founded by

    incoming NACE

    International Vice

    President Sandy

    Williamson and based in Calgary, Alberta,

    Canada, Ammonite provides corrosion en-

    gineering, materials selection advice, asset

    integrity management programs, evalua-

    tion of chemical treatment, and inspection

    programs for the oil and gas industry.

    Williamson will retain his current role as

    President of Ammonite. Cormetrics, Ltd.,

    managed by Frank Hornsby, provides fail-

    ure analysis, corrosion inhibitor testing,

    and crude corrosivity testing for the oil and

    gas industry. OEL Projects, Ltd. is an engi-

    neering, procurement, and project manage-

    ment contracting company headquartered

    in Calgary that serves the oil and gas indus-

    try in Canada.

    Sherwin-Williams Receives Military Coatings Project Award of Excellence The Sherwin-Williams Co. (Cleveland,

    Ohio) was awarded the SSPC: The Society

    measurement and/or control of hydro-

    carbon fluids. For more than 70 years,

    Francisco was an international leader in

    the design, manufacture, and calibration

    of turbine flow meters for rocket propul-

    sion and industrial fluid flow measure-

    ment applications. His engineering

    accomplishments and inventions have

    contributed significantly to the aerospace,

    as well as the oil and gas industries.

    Kapur Named President of Honeywell Process Solutions

    Honeywell (Morris

    Township, New Jer-

    sey) announced

    that Vimal Kapur

    has been named

    president of Hon-

    eywell Process

    Solutions (HPS), a

    Honeywell busi-

    ness that supplies automation control, in-

    strumentation, and services to process

    manufacturers in industries such as oil

    and gas; refining; pulp and paper; petro-

    chemicals; and metals, minerals, and min-

    ing. A near-30-year veteran of the process

    automation industry, Kapur has been with

    Honeywell for more than 25 years. He has

    held a number of key strategic business

    positions within Honeywell, including vice

    president of Global Marketing and Strat-

    egy for HPS and managing director for

    Honeywell Automation India, Ltd. (HAIL).

    Prior to this appointment, he was vice

    president/general manager of the Ad-

    vanced Solutions line of business for HPS.

    for Protective Coatings Military Coatings

    Project Award of Excellence, along with

    International Marine and Industrial Appli-

    cators, LLC (IMIA), for its work on the U.S.

    Navys USS Ronald Reagan (CVN-76). The

    award recognizes exceptional coatings

    work performed on U.S. military ships,

    structures, or facilities. In the seven

    months during the USS Ronald Reagans

    dry docking at Puget Sound Naval Ship-

    yard (Bremerton, Washington) in 2012 and

    2013, more than 17 acres (68,799 m2) of

    steel would need to be preserved on the

    ships freeboard; underwater hull; sea

    chests; cat walks; and various tanks, voids,

    and vent plenums. This project was the

    largest preservation project to have ever

    been completed at the shipyard.

    ISHM Announces 2014 Laurence S. Reid Award Recipient

    The International

    School of Hydro-

    carbon Measure-

    ment (ISHM)

    (Norman, Okla-

    homa) proudly an-

    nounces that

    Edward E. Fran-

    cisco, Jr. is the re-

    cipient of the 2014

    Laurance S. Reid Award, which was pre-

    sented posthumously. This award is

    presented each year in recognition of out-

    standing individual contributions to the

    U.S. Water Expands into Mid-Atlantic Region U.S. Water Services (St. Michael, Minnesota

    and Aberdeen, Maryland), a provider of

    integrated water and process solutions for

    industry, announces the acquisition of

    Water Chemical Service, Inc. (Waterchem).

    Waterchems Terry Bartley states, This acqui-

    sition is a game changer for us in the market-

    place. U.S. Water has a similar culture and

    attitude to Waterchem, as well as expanded

    service offerings and locations across the U.S. Well leverage and combine our strengths

    with U.S. Water to target the immense growth opportunities presented to us in the area.

    Were excited about what this acquisition will bring in terms of service and capabilities

    to our existing and future customers.

    MP welcomes submissions of

    Company News. Please send photos and

    information to Husna Miskinyar;

    e-mail: [email protected].

    NACE Incoming Vice

    President Sandy

    Williamson.

    21NACE INTERNATIONAL: VOL. 53, NO. 8 MATERIALS PERFORMANCE AUGUST 2014

    August 2014 MP.indd 21 7/21/14 12:50 PM

    mailto:[email protected]

  • Fire Safe Flange Isolation Kits

    PosiTector PC Powder Checker Now Available

    DeFelsko

    (Ogdensburg,

    New York) is

    pleased to

    introduce the

    next generation

    of non-contact

    powder thick-

    ness gages. The

    PosiTector PC

    Powder

    Checker

    measures uncured powder coatings

    using ultrasonic technology to auto-

    matically calculate and display a

    predicted cured thickness. The

    PosiTector PC helps to control powder

    consumption to ensure adequate cover-

    age and reduce waste. The updated

    PosiTector PC Powder Checker features

    a color liquid-crystal display (LCD), an

    expanded internal memory, and free

    access to a full suite of PosiSoft

    Solutions. The gage continually

    displays/updates basic statistics and

    automatically generates formatted

    reports with measurement summaries

    and charts. Notably, the PosiTector PC

    applications, says Wisdom Dzotsi,

    general manager, Quantum

    Com posites. The hybrid carbon f iber

    material, AMC-8590-12CFH, is an

    advanced molding compound that

    offers the performance benefits of

    carbon f iber at a cost similar to high-

    performance f iberglass. It is easily

    moldable, delivering parts that are high

    strength, low density, and resistant to

    fatigue. Tel: +1 989-922-3863, Web site:

    www.quantumcomposites.com.

    Hybrid Performance Precision Grout for ConstructionBASF (Shakopee, Minnesota) introduces

    a new product in North America de-

    signed for precision grouting of critical

    equipment. MasterFlow 4316 hybrid

    performance grout combines the

    strength of an epoxy grout with the ease

    of applying cementitious grouting ma-

    terials. MasterFlow 4316 grout is the

    newest addition to the Master Builders

    Solutions grout family, specified glob-

    ally as premier products for demanding

    applications such as compressors, gen-

    erators, pump bases and drive motors,

    tank bases, conveyors, and column sup-

    ports. The one-component grout is easy

    to mix, has low odor, and can be easily

    cleaned up with water. Tel: 1 800-526-

    1072, Web site: www.master-builders-

    solutions.basf.us.

    New 27MG Ultrasonic Thickness Gage

    Olympus (Waltham, Massachusetts) is

    pleased to announce the release of the

    27MG Ultrasonic Thickness Gage that is

    designed to make accurate measure-

    ments from one side on internally

    now accepts all PosiTector probes to

    easily convert from measuring uncured

    powder to cured dry film thickness,

    surface profile, and more. Tel: 1 800-

    448-3835, Web site: www.defelsko.com.

    First Hybrid Carbon Fiber Material

    Quantum Composites (Bay City,

    Michigan), a business unit of The

    Composites Group, introduces its f irst

    hybrid carbon f iber material, a cost-

    effective, lightweight, and high-

    strength alternative for traditional

    f iberglass and metal applications in the

    automotive, heavy truck, medical,

    sporting goods, and industrial markets.

    This new materialwith its improved

    f lexural and tensile moduli at a

    sig nif icant cost reductionhas created

    the opportunity for new thermoset

    Lamons (Golden, Colorado), a manufac-

    turer of fire safe f lange isolation kits for

    critical offshore platform and refinery

    applications, introduces the DEFENDER

    FSTM sealing/isolating gasket. The product

    is designed to withstand the rigorous API

    standard 6FB (Third Edition) test and

    therefore provides a solution for those who

    want to electrically isolate their f lange,

    provide a seal for media, and protect

    against the introduction of fire in and

    around the f lange. Available in ANSI, API,

    and PN pressure classes with a nominal pipe size range of through 36 in (13

    through 914 mm), the gasket utilizes a Kammprofile design with a standard Type 316

    (UNS S31600) stainless steel core (Inconel and duplex available upon request). Isola-

    tion materials are G10 or G11 and the Kamm profile seals are faced with Teflon and

    Mica seal elements. Tel: +1 303-405-6812, Web site: www.lamons.com.

    22 AUGUST 2014 MATERIALS PERFORMANCE NACE INTERNATIONAL: VOL. 53, NO. 8

    PRODUCT SHOWCASE

    August 2014 MP.indd 22 7/21/14 7:43 AM

    http://www.lamons.com/http://www.lamons.com/http://www.quantumcomposites.comhttp://solutions.basf.ushttp://www.defelsko.com

  • corroded or eroded metal pipes and

    structures. It weighs only 12 oz (340 g)

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    utilize the same technologies available

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    durable, rugged 27MG is battery oper-

    ated and features a large, backlit LCD

    with easy-to-read numerals, and an

    intuitive color-coded keypad with

    direct access to many key features.

    Tel: +1 781-419-3562, Web site: www.

    olympus-ims.com.

    New Metals from EOS

    EOS (Krailling, Germany) metals port-

    folio now includes new titanium and

    stainless steel (SS) for end-use produc-

    tion on its direct metal laser-sintering

    (DMLS) systems. Lightweight EOS

    Ti64ELI alloy has excellent corrosion

    resistance and biocompatibility plus a

    high grade of purity. It is extremely

    well-suited for the additive manufac-

    ture of medical implants for orthope-

    dics. EOS Type 316L SS (UNS S31603)

    combines corrosion resistance with

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    surgical instruments, endoscopic

    surgery, orthopedics, and implants.

    Parts built from the new steel have a

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    for SS bar and wire for surgical

    implants). The steel also has potential

    applications in the watch and jewelry

    industries, as well as in harsh and

    demanding environments such as the

    aerospace or marine industries. Tel: +1

    248-306-0143, Web site: www.eos.info.

    Intertherm 228HS for North American Market

    International

    Paint (Houston,

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    cas offshore

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    temperature-resistant epoxy phenolic

    coating offers higher solids and lower

    volatile organic compounds (VOCs) to

    provide improved protection to insu-

    lated steelwork. According to Chris Mc-

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    the many characteristics of Intertherm

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    PPG to Reintroduce DURANAR ADS Coatings for Architectural MetalsPPG Industries (Pittsburgh,

    Pennsylvania) coil and building prod-

    ucts coatings group announced that it

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    General Purpose Industrial Air Pressure Regulator Series

    Marsh Bellofram Corp. (Newell, West

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    marshbellofram.com.

    MP welcomes submissions of product press releases and photos for Product Showcase. Please send them to the attention of Husna Miskinyar, NACE International; tel: +1 858-768-0829; e-mail: [email protected].

    23NACE INTERNATIONAL: VOL. 53, NO. 8 MATERIALS PERFORMANCE AUGUST 2014

    The Latest Tools forFighting Corrosion

    August 2014 MP.indd 23 7/21/14 7:43 AM

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  • I

    FEATURE ARTICLE

    Updating NACE SP0169 for Controlling External Corrosion on Underground or Submerged Metallic Piping Systems

    In October 2013, NACE International

    released an updated version of SP0169,

    Control of External Corrosion on

    Underground or Submerged Metallic

    Piping Systems, which presents methods

    and practices for achieving effective

    control of external corrosion on under-

    ground or submerged metallic piping

    systems. The revision was accomplished

    by NACE Task Group (TG) 360, Piping

    Systems: Review of NACE SP0169-2007.

    This task group is administered by

    Specific Technology Group (STG) 35,

    Pipelines, Tanks, and Well Casings,

    and is comprised of corrosion control

    personnel from oil and gas transmission

    companies, gas distribution companies,

    water and wastewater utilities, power

    companies, corrosion consultants, and

    others concerned with external corrosion

    control of underground or submerged

    metallic piping systems. This is the fifth

    revision of the standard, which was origi-

    nally published in 1969. The previous

    revision was performed in 1992 by NACE

    TG T-10-1, and since then the standard

    was reaffirmed (without revisions) in 1996,

    2002, and 2007.

    SP0169 describes the use of electrically

    insulating coatings, electrical isolation, and

    cathodic protection (CP) as they relate to

    external corrosion control, and is intended

    to be used by corrosion control personnel

    responsible for pipelines that transport oil,

    gas, water, and other fluids, although the

    methods outlined in the standard are also

    applicable to many other underground or

    submerged metallic structures. Significant

    changes and additions were made in the

    2013 revision of SP0169, particularly in

    Section 5, External Coatings, and Section

    6, Criteria and Other Considerations for

    Cathodic Protection. Additionally, a review

    of potential criteria in national standards

    from around the world was added as an

    appendix.

    Kathy Riggs Larsen, Associate Editor

    Corrosion personnel perform nondestructive testing (magnetic-particle inspection) on an excavated portion of pipe. Photo courtesy of Drew Hevle.

    24 AUGUST 2014 MATERIALS PERFORMANCE NACE INTERNATIONAL: VOL. 53, NO. 8

    Aug14_Feature.indd 24 7/21/14 1:01 PM

  • Updating NACE SP0169 for Controlling External Corrosion on Underground or Submerged Metallic Piping Systems

    This is the standards fifth revision since its original publication in 1969.

    A corrosion technician inspects an excavated portion of pipe for coating damage and external corrosion. Photo courtesy of Drew Hevle.

    A pipe is recoated in the field with an airless-spray two-part epoxy coating, which protects it from external corrosion. Photo courtesy of Mears Group, Inc.

    25MATERIALS PERFORMANCE AUGUST 2014 NACE INTERNATIONAL: VOL. 53, NO. 8

    Aug14_Feature.indd 25 7/21/14 1:02 PM

  • FEATURE ARTICLE

    To learn more about the recent

    revisions made to SP0169 and their impact

    on industry, Materials Performance asked

    several members of NACE TG 360 and

    others interested in the standard revision

    to comment on the updated portions of

    the standard. Panelists are Jim Chmilar

    with Chmilar & Associates Consulting

    Ltd.; Drew Hevle with Kinder Morgan;

    Mark Lauber with Laclede Gas Co.; and

    Norm Moriber with Mears Group. (See

    their biographies in the sidebar, Meet the

    Panelists.)

    MP: How does industry use NACE

    Standard SP0169? Why is this standard

    important?

    Drew Hevle: NACE SP0169 is the

    de facto standard for CP of pipelines in

    the world, the first standard that NACE

    published, and one of the most influential

    standards issued by NACE. It contains

    sections on coatings, CP criteria, and

    the design, installation, operation, and

    maintenance of CP systems. Many regula-

    tory agencies reference this standard.

    For example, the U.S. Department of

    Transportation references the SP0169 CP

    criteria for its hazardous liquid pipeline

    safety regulations in the Code of Federal

    Regulations (49 CFR 195 Subpart H).1

    Mark Lauber: As an operations

    manager responsible for pipeline safety

    regulatory compliance for both steel

    natural gas distribution and transmission

    systems, I feel that SP0169 is a valuable

    technical document because it is a

    comprehensive resource for any pipeline

    owner who wishes to identify the neces-

    sary steps proven to adequately mitigate

    corrosion of these valuable assets. The

    standard is important for several reasons.

    It provides specific criteria where corro-

    sion control is expected to be achieved for

    stated conditions, and it provides perfor-

    mance language for pipeline operators

    who have documented empirical evidence

    indicating corrosion control effectiveness

    using other criteria. The standard also

    provides an enormous number of techni-

    cal references for coatings applications,

    Meet the Panelists

    Jim Chmilar

    Jim Chmilar gradu-

    ated with an en-

    gineering degree

    from the University

    of Calgary in 1972

    and started as a

    feld engineer do-

    ing cathodic pro-

    tection (CP) work with Associated Corro-

    sion Consultants Ltd. in Calgary, Alberta,

    Canada. He retired from that company

    in 2003 after 30-plus years and formed a

    one-man consulting company to enable his

    continued involvement with NACE Interna-

    tional. A NACE member since 1976, Chmi-

    lar has been the chair of various commit-

    tees, including Instructor and Peer Quality

    Committee, Quality Committee, Technical

    Practices Committee (TPC), Technical and

    Research Activities Committee, the Policy

    Committee, and Task Group (TG) 360.

    Chmilar received a NACE Distinguished

    Service Award in 1990 for section and area

    conference work, and was the recipient of

    the NACE R.A. Brannon Award in 2010.

    Drew Hevle

    D rew Hev le i s

    manager of cor-

    rosion control for

    Kinder Morgans

    natural gas pipe-

    line group, based

    in Houston, Texas.

    He has a Bachelor

    of Science degree in mechanical engi-

    neering and holds several NACE certi-

    fcations, including Corrosion Special-

    ist, CP Specialist, and Level 3 Coating

    Inspector. Hevle heads several NACE

    technical committees, is vice chair of the

    NACE Technical Coordination Commit-

    tee (TCC), and is also a NACE instructor.

    His hobbies are corrosion control and CP.

    Mark Lauber

    Mark Lauber is

    the manager of

    p ipel ine safety

    compl iance for

    the Laclede Gas

    Co., which serves

    eastern Missouri,

    including St. Louis,

    and western Missouri, including Kansas

    City. A NACE-certifed CP Specialist since

    1997, he is responsible for integrity man-

    agement programs for the companys

    gas transmission, gas distribution, and

    hazardous liquid pipelines. This includes

    corrosion control, main replacement,

    and public awareness programs. In ad-

    dition, Lauber has overall responsibility

    for pipeline safety regulation compliance

    for Laclede Gas. He holds a Bachelor of

    Science degree in electrical engineering

    from the University of Missouri-Rolla.

    Lauber is a member of several NACE

    technical committees, including TG 360.

    26 AUGUST 2014 MATERIALS PERFORMANCE NACE INTERNATIONAL: VOL. 53, NO. 8

    Aug14_Feature.indd 26 7/21/14 1:02 PM

  • Updating NACE SP0169 for Controlling External Corrosion on Underground or Submerged Metallic Piping Systems

    CP criteria from other standards around

    the world, and completed CP research.

    Norm Moriber: RP0169 was the first

    recommended practice developed by

    the National Association of Corrosion

    Engineers and was a critical document in

    establishing NACE as the world leader in

    corrosion prevention and control. This

    standard has provided the framework

    for pipeline integrity management plans

    since before that terminology existed.

    Engineers and operators have relied on

    RP0169 (and now SP0169) as a refer-

    ence for the industry consensus on best

    practices for corrosion control on pipeline

    systems.

    Jim Chmilar: Industry primarily cites

    the criteria in Section 6 for external corro-

    sion control of underground or submerged

    metallic piping systems. Some also find

    the accepted methods and practices

    covered in the other eight sections very

    useful for design, installation, operation,

    and maintenance of the corrosion control

    system they establish.

    MP: Why was it necessary to revise

    SP0169?

    Moriber: Technical Coordination

    Committee (TCC) procedures require that

    standards be reviewed every five years to

    determine whether they should be

    reaffirmed, revised, or withdrawn. This

    standard was revised in 1972, 1976, 1983,

    and 1992; and it was reaffirmed in 1996,

    2002, and 2007, which means it had been

    more than 20 years since it was updated.

    A blue-ribbon ad hoc committee reported

    in 2002 that revisions were required in

    several key areas, including clarification of

    CP criteria, better guidance regarding

    microbiologically influenced corrosion

    (MIC) and elevated-temperature corro-

    sion, and upper limits of protection to

    avoid cathodic disbondment of coatings

    and damage to high-strength steels. It was

    also recommended that information be

    provided on CP criteria used outside of

    North America in recognition of NACEs

    commitment as an international

    organization.

    Lauber: I believe it was necessary to

    revise SP0169 because pipeline opera-

    tors like me found the 850 mV criterion

    language to be confusing and unclear.

    Furthermore, because SP0169 was

    reaffirmed several times without updat-

    ing technical references to the advances

    in coatings and coatings standards that

    had been made in the last several years,

    the previous version of this standard was

    seriously dated.

    Chmilar: The previous revision of

    this standard occurred in 1992, thanks to

    Ted Kazmierczak and TG T-10-1. A STG

    05, Cathodic/Anodic Protection, ad hoc

    committee on Criteria Review in RP0169-

    96 presented a report at CORROSION

    2002 that stated: Section 6 could not be

    reaffirmed as it exists; ambiguity exists

    between the 0.850 vs. copper/copper

    sulfate (Cu/CuSO4) electrode (CSE)

    current-applied criterion and the 0.850

    vs. CSE polarized criterion; there are

    other international criteria that should

    be considered; there is confusion regard-

    ing 100 mV formation and decay; more

    guidance is needed on CP criteria for

    controlling MIC and corrosion at elevated

    temperatures; and upper limits on CP

    criteria for coating damage and/or high-

    strength steels are needed.

    STG 05 formed TG 285 in 2002 to

    revise Section 6. That TG had numer-

    ous meetings and conference calls and

    gathered significant information, but did

    not achieve its goal of getting out a ballot

    to the group and was disbanded in 2006.

    The task was turned over to TG 360 under

    STG 35 to review the entire document,

    including Section 6. Part of the NACE and

    ANSI protocol requires all standards to be

    revised or reaffirmed every five years.

    Hevle: The goals included updating

    the standard (last revised in 1992), clarify-

    ing the CP criteria, and adding guidance

    for special conditions such as alternating

    current (AC) corrosion, MIC, dissimilar

    metals, and high temperature. Other

    sections needed updates, as technology

    has changed in the last 20 years.

    MP: What are the major changes made

    during the latest revision?

    Lauber: Without question, I believe

    the criteria section has seen the most

    significant changes. The definitions

    section and coatings references have also

    been expanded greatly. Additionally, infor-

    mation on criteria and cautionary notes

    was enhanced for special conditions such

    as high-resistivity soils, MIC, high pH, and

    high-temperature environments.

    Chmilar: The major changes were in

    Section 5 and Section 6 plus the addition

    of abbreviations and acronyms to an

    updated definitions section. In Section

    5 on external coatings, there was signifi-

    cant work done to upgrade and update

    the standards lists with the addition of

    numerous coating types and a table for

    Norm Moriber

    Norm Moriber is

    chief engineer for

    Mears Group, In-

    tegrity Solutions

    Division, in San

    Ramon, California.

    He is a graduate of

    the Massachusetts

    Institute of Technology and a Registered

    Professional Corrosion Engineer in Califor-

    nia with more than 40 years of experience

    in the corrosion control industry. His areas

    of specialization include CP design and

    evaluation; external corrosion direct assess-

    ment, focusing on cased piping; and stray

    current evaluation and mitigation. He has

    served on the NACE International Board

    of Directors, as chair of the Public Affairs

    Administrative Committee, has been a

    member of the Materials Performance Edi-

    torial Advisory Board since 2001, and is now

    a technical editor for MP. He is a member

    of TG 360 and has chaired Technology

    Exchange Group (TEG) 179X, Cathodic

    Protection, since 2004.

    27MATERIALS PERFORMANCE AUGUST 2014 NACE INTERNATIONAL: VOL. 53, NO. 8

    Aug14_Feature.indd 27 7/21/14 1:02 PM

  • FEATURE ARTICLE

    ductile iron, plus additional references

    in Appendix A. In Section 6, there was a

    restructuring of the stated criteria and the

    addition of stainless steel (SS) pipe as a

    pipe class. There are Special Conditions

    and Relevant Considerations listed in

    Section 6 that deal with issues such as

    MIC; elevated temperatures; high-resis-

    tivity electrolyte; mill scaled steel; mixed

    metal piping; high-voltage AC (HVAC);

    weak acid environments; stress corrosion

    cracking (SCC); hydrogen embrittle-

    ment (HE) and blistering; and electrical

    shielding. There is now a figure showing

    corrosion rates as a function of AC with

    CP current densities and a figure on SCC

    range. There is now a statement that

    potential measurements related to criteria

    are intended to be made at 25 C (77 F)

    and a table for correction factors where

    reference electrodes are not within 10 C of

    25 C. There are eight pages of references

    and a bibliography where more detailed

    information can be located. There is now

    an Appendix B, Review of International

    Standards, which is a summary of inter-

    national and country standards as they

    relate to CP criteria.

    Hevle: Many needed changes were

    made, and all the sections were updated.

    The most controversial change was made

    to the CP potential criteria section on

    how voltage drop errors are addressed.

    Previous versions of this standard had

    a number of variations to the wording

    regarding how these errors are to be

    addressed. This version uses the original

    language, consideration of the signifi-

    cance of voltage drops.

    Moriber: There has been a major focus

    on the CP criteria for steel piping systems,

    and that is an important part of SP0169;

    however, it is by no means the only section

    where critical upgrades have been accom-

    plished. CP criteria for steel and gray or

    ductile cast iron have been clarified and

    greater flexibility is now available for

    operators to make choices that will meet

    their corrosion control objectives. New

    sections have been added to address CP

    for copper, aluminum, and SS, along with

    cautions about additional requirements to

    address specific conditions. These include

    MIC, high temperatures, SCC, overpro-

    tection and hydrogen evolution effects,

    dissimilar metal piping systems, acidic

    and high-resistivity environments, electri-

    cal shielding, and AC corrosion. Because

    this standard addresses corrosion control

    rather than CP alone, the section on

    protective coatings was greatly expanded

    and updated. This includes the removal of

    references to numerous obsolete coating

    standards and the addition of modern

    coatings for steel and ductile iron. Other

    sections address a variety of reference

    electrodes and temperature correction for

    potential measurements. New appendixes

    describe CP criteria and other features

    contained in ISO and European standards

    in addition to those used in six other

    countries.

    MP: Why are these changes significant?

    Chmilar: The changes to the 2013

    version are really a change from the last

    major revision completed in1992 by

    Kazmierczak and TG T-10-1. The changes

    outlined in my previous answer provide

    additional resource information and

    the coating information has also been

    updated. One general criteria statement

    was added, but the 2007 criteria were not

    changed other than combining two 850

    mV criteria into one stated criterion. The

    standard does not contain actual test

    methods as there is a specific test method

    (TM) for that purpose [TM0497-20122].

    This TM was first issued in 1997 and

    revised in 2012.

    Hevle: The changes reflect the consen-

    sus standard practices of the industry. In

    many ways the standard has changed to

    recognize new technologies. The provi-

    sions of any standard must be applied by

    competent persons, and it is impossible

    to write a standard so inflexible that it

    cannot be misapplied without compromis-

    A CP technician checks the rectifier outputs for a cathodically protected pipeline. Photo courtesy of Mears Group, Inc.

    28 AUGUST 2014 MATERIALS PERFORMANCE NACE INTERNATIONAL: VOL. 53, NO. 8

    Aug14_Feature.indd 28 7/21/14 1:02 PM

  • Updating NACE SP0169 for Controlling External Corrosion on Underground or Submerged Metallic Piping Systems

    ing technically sound applications.

    Moriber: These additions and

    updates restore one of NACEs signature

    standards to the level of quality that the

    world has come to expect of the leading

    corrosion control organization. SP0169

    now includes a wealth of new informa-

    tion and references to related documents

    that provide valuable guidance for those

    responsible for pipeline integrity. This

    standard will also be linked with the next

    revision of TM0497, the TM standard that

    will complement the clarifications to the

    CP criteria. These documents, together

    with the summaries of other internation-

    ally recognized standards, will provide

    options and flexibility that will allow

    operators to customize the procedures for

    achieving their corrosion control

    objectives.

    Lauber: I believe that the ambigu-

    ity surrounding the 850 mV criteria in

    the previous standard version has been

    eliminated. The listed criteria calling for

    a structure-to-electrolyte potential of

    850 mV or more negative gives opera-

    tors a roadmap that includes clear steps

    that must be taken for interpretation if a

    current-applied measurement is used.

    MP: How will these changes impact

    industry? How will they impact your

    organization?

    Hevle: Presently my organization

    (Kinder Morgan Natural Gas Pipelines)

    is not directly affected, because the U.S.

    natural gas pipeline safety regulations do

    not reference this standard, but indus-

    try consensus standards are extremely

    valuable. Standards codify and improve

    industry practices and allow a common

    language. They make pipelines safer and

    more reliable by incorporating expertise

    and experience from across the industry.

    Standards reduce costs by