The Benefit And Limitations Of Corrosion Coupons
The corrosion of steel piping and its related components is a continuous and virtually unstoppable process. The end product, which is commonly referred to as rust, is simply the result of an electrochemical reaction through which the higher energy processed metal is slowly reverted back into its naturally occurring chemical form – metal ore.
Even with the proper application of available countermeasures, the estimated cost for repairing corroded piping systems in the United States alone stands well in excess of $76 billion annually – making corrosion one of the most potentially damaging losses to any commercial, private, or industrial property next to fire. An estimated one sixth of all steel production worldwide is used to replace corroded metal – much of it at cooling and process water piping systems.
Different Testing Methods
While various options exist, such as ultrasonic testing, metallurgical analysis, spool pieces, and instantaneous electronic measurement (LPR), corrosion coupons still remain the most widely used and respected form of corrosion measurement and monitoring. Corrosion coupons are carefully machined small thin bars of various metals, typically mild carbon steel, which are inserted into an external “coupon rack” or zigzag layout of piping to the main circulating loop.
Some racks are made of steel pipe, and especially in areas of higher operating pressures. More commonly today where pressure permits, pre-fabricated coupon racks from PVC or plastic are installed.
The coupon itself is pre-weighed by the manufacturer to an accuracy of four decimal places before installation, and typically left in place for a duration of between one and six months. It is installed on a plastic or phenolic post which electrically insulates it from the rest of the piping assembly. Often multiple coupons are installed into the same rack, or dual examples of steel and copper. In some examples where a corrosion consultant is involved, multiple corrosion coupon racks may exist.
After exposure, the coupons are removed and returned to the place of purchase, corrosion consultant, or sent to an independent laboratory for analysis. Longer or shorter test periods may apply.
Exposed coupons are typically photographed as received, cleaned of any attached debris and deposits, visually inspected, dried and re-weighed, and then photographed again to show surface conditions. The corrosion rate of the coupon in mils per year (MPY) can then be estimated based upon the weight of material lost over its time in service. It is a weight derived calculation relating to all 6 surfaces rather than a true wall thickness loss measurement.
A large variety of metal alloys are available in various physical configurations, although for HVAC and process cooling applications, rectangular bars of 1010 and 1018 mild carbon steel and soft copper are the primary materials used.
Benefits Of Coupons
Corrosion coupons offer confirmation that chemical treatment is present to any building owner or plant operator. If monitoring is continuously maintained and a history of coupon test results accumulated, fluctuations in corrosion activity may be visible. Though limited in many respects, coupons will often provide the only indication of corrosion status, and the only inside look at the conditions and type of deposits existing within a piping system.
Corrosion coupons become an even more valuable predictive maintenance tool when results are compared to confirmed wall loss information – such as provided through ultrasonic thickness testing, spool piece measurement, or actual pipe removal and metallurgical analysis. Where regular testing under rigorously controlled conditions exists, corrosion coupons will provide an excellent indication of whether the potential for corrosion to occur is increasing or decreasing.
Corrosion coupons will quickly document if a chemical inhibitor is present by an absence of significant wall loss, or similarly show whether the recommended inhibitor is effective for providing protection to a particular metal. Another great benefit is to provide short term corrosion rate data, such as might be required during a harsh chemical cleaning or chemical program evaluation.
Due to a wide variety of reasons, however, corrosion coupons generally fail to produce corrosion rate values relative to actual pipe wall loss. At best, they offer an estimate of the corrosivity of the fluid, rather than a measurement of the true metal lost from the pipe.
The most of the severe corrosion related piping failures we have investigated, such as the condenser water piping system at left, corrosion had been allowed to continue due to the very favorable corrosion coupon rates reported.
In many cases, most notably illustrated by the case history at left, even the most obvious indications of a corrosion problem such as rust deposits, clogged strainers and condenser tubes, and even leaks, have been ignored or discounted due to favorable corrosion coupon testings showing no problems whatsoever.
Sources Of Inaccuracy
Corrosion coupons commonly under report corrosion activity by 10 times or more. In many examples we have documented an under reporting inaccuracy of 2,000% and greater. Some of the many factors limiting the accuracy of corrosion coupons are:
Coupon Rack Placement
The corrosion coupon rack itself, installed externally to the piping system, limits many of the influences acting against any circulating water system. Variations in water flow can dramatically influence corrosion estimates by as much as five to ten fold. In addition, materials of construction, rack layout, pipe size, or filtering of the coupon rack assembly can significantly alter corrosion rate estimates.
Test layouts constructed of PVC will greatly eliminate any possible galvanic activity. Even the physical location of the coupon rack itself, at the top or bottom of the system, can produce significant differences in measured corrosion rate.
With no water flow available, corrosion coupons cannot be used to measure the always higher corrosion activity occurring during a winter lay-up or periodic drain down – documented in many cases to reach ten times that of water filled pipe. The exact same 12 in. piping system, having a wall thickness of 0.335 in. where filled, can actually show only 0.125 in. at the roof where drained over 20 years.
Yet with only the water filled area tested, this potential for failure will always remain hidden.
What degree of corrosion activity may exist is greatly dependent upon the type of piping system involved. Closed systems typically show the lowest corrosion and pitting activity, while open condenser or cooling tower loops show the highest.
An open circulating system also typically exhibits the greatest fluctuation in test result – which means that wall thickness is more likely to vary from top to bottom, at large and small pipe, at supply and return, and at other extremes of the system.
This increases the risk that any corrosion coupon testing performed at one area is not representative of the overall system.
By definition, corrosion is an electro-chemical reaction. But since corrosion coupons are typically isolated from any metal to metal contact through the use of a center located plastic or galvanic insulator, they are totally unaffected by the many anode/cathode electrochemical reactions always present in an established piping system.
The well recognized steel pipe to brass valve or copper pipe effect is a common example of galvanic forces which always exist to some degree in most piping systems. Lesser galvanic forces exist where different steels meet as well.
As a result, the major corrosion mechanism responsible for a significant amount of material loss is never measured.
No Flow Conditions
Some of the most severe corrosion and pitting conditions are found at areas of no flow. This is common at by-pass lines, future lines, lead and lag equipment, out-of-service equipment, as well as at the very end of some small diameter piping distribution systems.
Cooling tower by-pass lines, closed at the downstream end and open at the supply side, are notorious for providing a settlement area for deposits, and then very severe pitting underneath. With no flow available, corrosion coupon testing is, by definition, impossible – leaving the most vulnerable areas of the entire piping system un-addressed.
The typically mirror smooth polished surface of a corrosion coupon minimizes the adhesion of iron oxide, dirt and micro organisms. As a result, they are rarely attacked in the same manner as an aged piping system having an irregularly worn and pitted interior surface.
For an older piping system typically worn and pitted, new corrosion coupons bear no resemblance to the pipe surface – thereby further amplifying reporting error.
The most common test interval for corrosion coupons is between 30 and 90 days. In reality, 30 days is too soon for the coupon to develop a passivating layer of rust protection and can actually lead to the reporting of falsely high corrosion rates.
On the opposite end, 90 days is far too short of a time period necessary for the smooth surface of the coupon to accumulate any microbiological or deposit buildup typically existing in an actual piping system.
Both scenarios are well recognized and accepted as factors in the under reporting or over reporting of corrosion activity using corrosion coupons as a test method, yet are all too often used to explain away a high or elevated test result.
Low corrosion rate results are rarely, if ever, questioned.
By far, the accumulation of interior deposits, or lack thereof, is the greatest limitation to accurate corrosion coupon testing.
Once a solid layer of iron oxide or scale deposits adhere to the pipe’s interior, an entirely new set of corrosion mechanisms typically form which simply cannot be duplicated, nor measured, by any remotely located corrosion coupon.
For that reason, most authorities recognize that as pipe surface deposits increase, the correlation between the actual corrosion rate and the corrosion coupon measured rate significantly decreases.
Mild deposits will, depending upon their thickness, impede contact of the water treatment chemicals to the base metal, and therefore reduce their effectiveness to some degree.
Heavy deposit buildup, will, however, contrary to the claims of chemical treatment providers, isolate the pipe from any chemical protection whatsoever. This often results in random areas of pipe having deep wall loss – often at the lowest areas of the system and at long horizontal runs. Smallest diameter piping is especially vulnerable.
A 5 MPY corrosion rate against 12 in. schedule 40 steel pipe, for example, will actually remove 64 lbs. of metal into the circulating system for every 100 linear feet of pipe, and for every year of service!
Oxidized, this same steel reverts back into approximately 2.6 cu. ft. of iron oxide that will settle into the system if not filtered out. And while an open cooling tower system may flush some of those deposits away or at least signal a corrosion problem, closed systems hide their problems.
Secondary Corrosion Problems
Accumulated internal deposits often create a localized and severe secondary metal loss known as “concentration cell” or “oxygen cell” corrosion, and may create conditions favorable to micro biologically influenced corrosion or MIC.
While the volume of metal lost in MPY may be often viewed as acceptable, often overlooked are the consequences of high volumes of iron oxide settling into the piping system.
For any circulating system, therefore, the removal of all interior pipe surface deposits should be a priority.
It is our opinion (as well as of others) that it is virtually impossible to provide adequate corrosion protection to any piping system already heavily fouled with iron oxide deposits, and that the preliminary and total removal of such deposits is fundamental to reducing high corrosion and pitting rates.
Should corrosion coupons remain in place for sufficient time to deteriorate toward the surface texture and condition of the actual pipe and accumulate deposits, they are rarely re-weighed and returned in that worn and pitted condition. Instead, they are typically replaced with new test coupons and the entire testing process started over from the very beginning.
This unfortunately negates monitoring one of the most important contributors in all examples of high corrosion loss – the pitted and irregular interior pipe wall surface.
Further Coupon Error
- Too long or too short of a test interval
- Varying time intervals between successive tests
- Seasonal or water temperature variations
- Actions of the operating engineer
- Different corrosion coupon manufacturers
- The use of different corrosion coupon alloys
- Surface texture of the corrosion coupon
- Fraud and tampering of the testing process or of the coupon itself
- Differences in lab analysis procedures, coupon handling, and preparation
In a majority of ultrasonic investigations CorrView International, LLC has been involved, a property owner or plant operator will, for years, mistakenly believe they have a corrosion rate of well under 1 MPY based entirely upon corrosion coupon results. In fact, wall losses may actually be 5 MPY and significantly above. Reported open system corrosion rates under one tenth of a mil per year are not uncommon for corrosion coupon testing, yet are not even remotely feasible.
Often, when presenting conflicting MPY statistics between corrosion coupons and ultrasonic testing, building or plant owners and operators will choose to rely on the less reliable coupon based information. Wishful thinking perhaps, and an often mistaken and regretted decision after true corrosion losses have been confirmed.
The sudden appearance of a leak, rust deposits, chip scale, or other operating problem ultimately signals a corrosion condition hidden over an extended time, and further investigation begins. Unfortunately, this is usually discovered only after years of concealed and under reported piping damage.
Overall, corrosion coupons offer some diagnostic information, though with very clear limitations. In many examples, the information they provide is virtually worthless. A comparison of results to other more direct and more reliable testing methods, therefore, is always recommended.
The Leading Cause Of Pipe Failure At Condenser Water Systems
Despite various corrective measure, advanced failures at condenser water systems are on the rise. Many problems are engineered into the system from the start due to the failure to recognize the impact rust deposits and particulates have on producing higher secondary corrosion levels. In addition, most corrective measure, if they are attempted, fail to provide a solution. Here is why.
Undersized Steel Pipe
A Simple Dial Caliper Measurement Of New Steel Pipe May Reveal Surprising Results
In addition to the many corrosion influences negatively impacting piping systems, many new building properties are constructed using carbon steel pipe which is below factory specification. To the surprise of many, an FM or UL approval, like its ASTM stamp, does not define that the pipe actually meets ASTM thickness standards.
The Decline In The Quality Of Today’s Piping Products Means Greater Corrosion Problems
A large number of negative influences have comined to produce a higher frequency of corrosion problems – often in spite of all precautionary measures taken. Of those, lower quality pipe, undersized pipe, more complex piping layouts, and generally less effective chemical treatment options have produced a “Perfect Storm” contributing to more piping failures.
When Pipe Corrosion At A Fire Protection System Can Cost Lives
The time to learn of a fire pipe corrosion problem is not during an actual fire emergency. Internal rust deposits can, and have, totally blocked water flow through the sprinkler heads – resulting in the loss of human life. More common at dry systems, internal deposits are a serious threat to all fire protection systems.
Fire System Failures
Major Misconceptions Within The Fire Protection Industry
Ignoring the obvious does have serious consequences when it comes to fire protection systems. From the use of thin wall schedule 10 & 7 pipe, to lower quality pipe products, to frequent flow testing which brings in new fresh water, clear and well documented reasons exist to explain the higher corrosion activity found at today’s fire protection systems.
Fire System Corrosion
The Threat Of A High Corrosion Condition To A Fire Sprinkler Line
Often viewed only in terms of water damage in the case of a corrosion induced pipe failure, far more serious concerns exist, although rarely considered. Unlike HVAC piping systems, corrosion activity at fire related piping can impede and in some cases totally block water flow – a potentially life threatening condition during any fire emergency
The Benefits of Ultrasonic Testing in Determining Corrosion Rate and Service Life
Ultrasonic testing provides the most comprehensive, accurate, and cost-effective tool to assess the condition and remaining service life of any piping system. Planned and performed properly, ultrasound offers the first step toward identifying a potential corrosion problem, or for certifying a piping system as fit for service.
Why Not All Pipe Failures Are The Fault Of Your Chemical Water Treatment Provider
Various design elements to any piping system can have dramatic impact upon its corrosion activity. Pipe origin, schedule used, physical layout, and many other unknown factors can produce a pipe failure. And yet they are completely beyond the realm of protection offered by chemical water treatment.
Corrosion By Design
Pipe Corrosion Problems No Water Treatment Program Can Protect Against
Various changes have occurred to mechanical piping designs over the past few decades, with virtually all HVAC, plumbing, and fire protection systems having been affected in some way. Many changes relate to the materials themselves. Major changes in piping design, however, have introduced new corrosion problems no chemical treatment program can stop.
The Benefits and Limitations of Corrosion Coupons
Relied upon for decades as an indicator of corrosion activity within piping systems, corrosion coupons are highly unreliable in most examples, and totally worthless in others. Many of the most damaging corrosion failures have occurred while at the same time corrosion coupons produced excellent results. Here is why.
If Corrosion Activity Is Only 0.4 MPY, What Is Wrong With The Above Picture?
Corrosion coupons reported a 0.4 MPY corrosion rate for 6 years where the actual rate exceeded 25 MPY. Believed implicitly in contrast to multiple leaks and failures, the slow but total destruction of the entire condenser water piping system was the net result. A case history illustrating the threat from relying exclusively upon this highly flawed testing method.
Dry Fire Sprinkler
Fire Protection Contractor – Antifreeze: The Fine Line Between Hero and Defendant
Antifreeze used in dry fire sprinkler systems may solve one problem, but has also proven deadly. Rated a Class 1 flammable liquid, antifreeze can accelerate a fire, create a fireball, and even cause an explosion. Although now restricted to lower concentrations, antifreeze still adds heat value to any fire and introduces new and unknown liability to any such system.
American Welding Society – Understanding Pipe Corrosion Problems
A piping system that satisfies service life demands, requires the recognition of piping design vulnerabilities, effective corrosion monitoring, and the adoption of corrective measurements. With corrosion related failures on the rise, and with generally lower quality pipe being installed, advanced planning and an awareness of potential threats becomes more important.
World Pipelines – Investigation vs. Procedure
Substantially different findings are likely where ultrasonic pipe testing is approached as a forensic investigation based upon known system problems and vulnerabilities, rather than simply a linear based measurement procedure. A critical importance is understanding the inherent corrosion related problems to various piping systems. An adapting investigation will also produce a more definitive answer to any piping problem.
Fire Pipe Corrosion
Fire Protection Contractor – When Pipe Corrosion In a Fire Protection System Can Cost Lives
The time to first learn of a pipe corrosion problem is not during a true fire emergency when lives are in jeopardy. Thinner pipe, more corrosive steel, lower quality galvanizing, foreign pipe, dry systems, MIC – all such negative factors are driving toward higher internal corrosion deposits to render your fire protection system worthless.
Fluid Handling Systems – Finding The Remaining Service Life
Ultrasonic testing is, by far, the most informative diagnostic method available for determining pipe status, as well as extremely cost effective. An effective piping analysis is much more than a spreadsheet of a few wall thickness measurements – requiring careful statistical analysis and practical interpretation of the data.
World Pipelines – Multiple Metering And Monitoring Needs
With no single form of corrosion monitoring capable of proving full coverage to the many different forms of pipe corrosion possible, multiple testing methods are always advised. These should include ultrasonic testing, spool pieces, LPR, regular internal inspection, and a close observance to the often obvious but missed signs of a problem.
A 30+ Year Knowledge Base
Unfortunately, the above is a very common progression of events for many of our clients. Often, greater attention to chemical corrosion control and corrosion monitoring could have saved the system and avoided the problem. In others, a decades prior design flaw or poor choice of pipe supplier may be traced back as the primary fault.
During the 20 years that we have been involved in the field of ultrasonic pipe testing / corrosion monitoring, we have authored various Technical Bulletins for the benefit of our clients. These Technical Bulletins address frequent problem issues to any building owner or operator, and offer both insight as well as reasonable and proven solutions.
We offer below the various categories available, and continue to add new bulletins as time permits.
Interior Rust Deposits, Common Threats, Corrosion Types, Winter Lay-Up, MIC, Corrosion Monitoring and Testing, CUI, Corrosion Coupon Failures, Rust Removal, Reducing Corrosion Threats, Roof Level Corrosion, Drained Pipe, Corrosion Trends, Fire Sprinkler Corrosion, Corrosion At “Free Cooling” Systems
The Impact Of Flow Rate To Higher Corrosion, Inadequate Water Filtration, Piping Layout Design, “Green” Piping Designs
Corrosion Threats, Design Misconceptions, Interior Rust Deposit Threat, Dry Fire System Corrosion, Schedule 10 Pipe, Premature Failures, Clogged Fire Systems, Chemical Control Options, Remediation Choices
Condition Assessment, Due Diligence, Preparation Prior To Renovation, System Evaluation, Expert Witness
Heat Exchangers, Benefits of UT Testing, High Pressure Water Jet Cleaning, Filtration Errors, Chemical Treatment, Condenser Tube Coating, Mold Concerns, Chromate Removal, Growing Threat of Corrosion, Heat Exchanger Tub Coating, Nondestructive Testing
Schedule 40 Limitations, Piping Trends, Hidden Corrosion Threats, Dielectric Insulators, Clamped Grooved Piping, Piping Schedules, Pipe Testing Specification, Roof Pipe Draining, Low Corrosion Guidelines, Dual Temperature Piping Failure
Cold Water Threats, External Corrosion Issues, Fire Reserve Tanks, Interior Pitting, Protective Coatings, Rehabilitation
Improving Heat Transfer Efficiency, Improving Filtering Efficiency, Filter Placement, Poor Performance Causes, Filter Selection Considerations
Chemical Treatment Challenges, Limitations to Water Treatment, Corrosion Coupon Reliance