TABLE OF CONTENTS CONTACT US DOWNLOAD THIS PAPER (PDF)![]() |
Improvements in Offshore Pipeline Cathodic Protection & Life Extension Jim Britton |
||
| Abstract | ||
| New deep-water discoveries combined with current high energy prices have given much of the world's aging offshore infrastructure a new lease on life. Offshore pipelines in particular are at the highest risk of catastrophic external corrosion failure if their cathodic protection systems are allowed to fall into disrepair. Newly developed survey methods combined with innovative design software and low cost, easy to install hardware, are helping take the pain out of these life extensions for many operators worldwide. This paper briefly presents some case histories and discusses the methods used and the overall strategy driving them. The deep-water revolution is also presenting challenges in offshore pipelining. New methods for cathodic protection and simplified life cycle monitoring in a truly cost effective package are presented. | ||
| Introduction | ||
| The methods for cathodic protection of offshore pipelines have not changed very much in the last 40 years; this is surprising since every other aspect of offshore pipelining has undergone radical improvement over the same time period. Coatings have evolved from old mastic based systems to ultra reliable three layer systems, thermally insulating coatings etc. The old lay barges have been replaced with sophisticated purpose built pipe lay vessels, pipes can be reeled and laid with maximum efficiency. Must have been that the CP guys were the only ones to get it right from day one? Obviously not, the bracelet anode has a mass of shortcomings; the only reason it hasn't changed is because it has been accepted into offshore lore. We are about to see that a change is just around the comer, after 40 years + we are due! The writer's company has been at the very forefront of this industry for the past two decades, this paper shows the future of, and will dispel many frequent misunderstandings about offshore pipeline external corrosion control. | ||
| Pipeline Survey Inspection and Monitoring | ||
| This area is one of the writer's "pet peeves" regarding our industry. The early days of
doing CP surveys on offshore pipelines (1970's predominantly) borrowed directly from
onshore methods and came up with the dreaded tow fish trailing wire survey. The flaws
of which are clearly understood by all, however the lore-thing works here too. Millions
of dollars have been wasted by operators trying to get meaningful information using this
method. To now admit that it was all a waste of time and effort is difficult for many who
have either misled or have been misled, but the fact, like it or not, is that the data are
worthless and often times dangerously optimistic. But take heart, most pipelines were
not at serious risk for the first 25-30 years of their life anyway. The first time a technically
correct method is used, a sound baseline for future integrity management is established,
and those old data no longer have any value at all. |
||
| How should it be done? | ||
| The ROV assisted three-electrode technique was pioneered in the North Sea in the late 70's
and early 80's. It was the first time true close-interval offshore potential data were
available; it is now the most widely used survey method for areas where an ROV can be
used effectively, and when correctly calibrated produces the most accurate data available.
Whether or not it is necessary to gather this much data or spend this much money to
verify the condition of a pipeline CP system is arguable. |
||
| What options are there? | ||
| The options that are available are driven by the amount of information required. If a
potential reading is required at 1-meter intervals along a pipeline then you are stuck with the ROV and three-electrode approach. How about a data point every
200 meters, or a data point every 10 Km? Could this be enough information? The answer
is "yes," provided that it's the right type of information. Short order changes in protection
levels of coated offshore pipelines are very predictable and do not occur in the same way
that they can onshore. This can be verified by analysis of the tens of thousands of miles
three electrode data that has been processed over the last quarter of a century. In truth, we
can make accurate assessment of a pipeline CP system with a relatively few accurate and
repeatable data points. This ability is further enhanced is there is an accurate baseline
survey available. The CP Snake is a BLF survey method (Bottom-towed, Lateral, Field gradient). Using the same basic 3-Electrode methodology but making lateral intersects with the pipeline and running on the seabed. With this method, an accurate data point is obtained at whatever interval the operator requires but generally 200-300 meters spacing. This is enough data to positively verify the pipeline cathodic protection status. The nature of the BLF survey ensures an accurate and verifiable data point unlike the old trailing-wire tow-fish method, and offers that same general low cost. Depending on local diver / ROV costs, another option is to take periodic subsea contact potentials at reasonable distance intervals, or to install permanent monitors at key locations and read with divers or low cost ROV's. The extent to which these methods can be usefully employed depends upon the particular pipeline and the local regulations. The important point is that it is not necessary to have thousands of data points to do the job. Recently updated pipeline design codes (ISO, DnV, NACE) stress the importance of attenuation modeling as a design aid. Attenuation models predict the potential distribution along a pipeline at various distances from known CP current sources attached to the pipeline. This fact can be put to work not only during design of the pipeline but also during the life cycle maintenance of the pipeline. Thus it is fully acceptable to predict the worst case potential at the mid point between two known current source drain points. This fact can be put to good use when a pipeline is retrofitted with intermittent anode sleds. Once we have measured the potential at the drain point (point of connection of the anode sled to the pipeline), the mid point pipeline potential between sleds and the current output (EFG) associated with each sled, we have a good baseline from which to develop a life cycle maintenance/survey program. Interval surveys need only consist of drain point measurements; potential attenuation modeling will do the rest. |
||
| Attenuation Modeling | ||
| There are a number of critical variables, which will affect the accuracy of any model.
These variables occur on both sides of the reaction: Key Cathodic Variables |
||
| 1. Coating condition, size, number and linear distribution of coating defects.
(Most models either assume worst case or linear distribution of damage at a
given coating breakdown percentage) 2. Pipeline material and wall thickness. 3. Pipeline operating temperature. 4. Exposed or buried. (Most models assume worst case (pipeline exposed, anodes buried)) |
||
| Key Anodic Variables | ||
| 1. Anode array to environment resistance, including connection resistance. | ||
| A successful model derives input from a logical analysis of the situation, this means putting into the model what we believe to be the true condition of the pipeline and its anode system. For new pipelines this is relatively easy, for old pipelines it can be easy if we have accurate and meaningful survey data. The application of attenuation models in offshore pipeline retrofit design is critical to keep the costs of this type of work under control. When one considers that the cost of a pipeline retrofit offshore is virtually directly proportional to the number of dives that have to be made it is clear that optimization of sled spacing offers a significant benefit. | ||
| Retrofitting an Existing Offshore Pipeline | ||
| Forward thinking operators in many areas of the world are realizing the value of offshore
pipelines. Not only as a high integrity transport to support ongoing oil and gas operations,
but as an in-place conduit that could be used for other energy related purposes in the
future. Given that the cost to maintain the pipeline in good condition for decades at a time
is relatively low, there are many offshore pipeline CP retrofit initiatives worldwide. There are three main reasons to retrofit and maintain offshore pipelines against external corrosion. |
||
| 1. The original system has depleted, and the integrity of the pipeline has to be
maintained. 2. The pipeline will be required to serve beyond its original design life. 3. Damage to the coating or anode systems either during or post installation. | ||
| The methodology to follow is basic: | ||
| 1. Assess the condition of the pipeline. There are optional strategies to follow. [1] 2. Calculate CP requirements and develop anode array physical design and optimized spacing on the pipeline. 3. Define connection method for connecting anodes to pipeline. 4. Install system. 5. Baseline post-retrofit survey (this is the NEW baseline, all previous survey data are of NO VALUE at this point.) |
||
| The writer's company has completed many successful pipeline retrofits based on all of these reasons. The projects have been completed with ROV's and divers very efficiently. The keys to the success of this method are: | ||
| 1. Proven attenuation model packages. 2. Using only accurate survey methods. 3. Anode sled designs optimized for any condition of current, life, installation method and ocean bottom condition. [Fig. 1] 4. Reliable ROV or diver anode sled connection systems. Systems that eliminate the need to fully expose the pipeline or to remove any concrete weight coating. [Fig. 2] 5. Simplified life cycle maintenance options. |
||
| Case History Summary | ||
| 12" Oil Pipeline 35 Miles Long (Gulf of Mexico) Retrofitted 2000 Saturation dive spread operating from 4-Point DSV. 225 feet sea-water max. 60% of pipeline buried> 3 feet. 14 Dual Sled Installations installed at approximately even spacing on pipeline. Installation Time: 7 days Project Cost: $415,000.00 |
||
| New Pipelines in Deep Water | ||
| Pipelines in deep water should not be treated like pipelines in shallow water. There are key differences that translate into obvious key strategy changes when dealing with the subject of corrosion control. | ||
| 1. The better quality the coating on the line can obtain the easier it is to maintain
long-term corrosion protection. Thus installation of bracelet anodes is completely
counter-productive in so much as the coating is unnecessarily compromised at
every anode installation (hundreds of sites on a 20 Mile pipeline). Moreover
anode attachment often requires an interruption in the lay procedure, which
translates to higher installation cost and reduced efficiency. 2. If we get a 99 percent efficient coating on bottom we can use a variety of smart (self monitoring] CP systems to protect miles of pipeline from a single easily monitored installation. This capability is further enhanced in deep water, since anode structures can be engineered to operate in the water phase, [Fig 3] rather than getting buried in the mud (with all the inherent loss of efficiency). 3. Deep water pipelines often have special coatings for thermal insulation. It is most undesirable to violate these coatings for the purpose of anode attachment. Pre-installed anode connection rings can be engineered into a field joint to provide a ROV post install tie back every 5 miles or so for a smart anode array. |
||
| In realization of these points, recent updates to the relevant codes of ISO and DNV recognize these methods as appropriate, and they have design guidelines for remote anode CP systems and new pipeline coating efficiency rules to correspond. | ||
| Summary | ||
| Ensure that all elements of your asset integrity program are reliant on unquestionable survey information. Utilize the newest technology available to provide efficient and verifiable CP performance. For new construction focus on high performance coatings with scaled back widely spaced smart CP stations Gust like the onshore guys). | ||
| References | ||
| 1. J. Britton "Offshore Pipeline Retrofit Strategies" CORROSION?? Paper No. | ||
| Figures | ||
| Figure 1: Sacrificial Anode Sleds for Offshore Pipeline Retrofit RetroSled - Rigid Sled for Pipeline Retrofit. Use on firm, sandy bottom. Low scour tendency. 3-4 Amps output. (click here for more info) ![]() Expanding RetroSled - Articulting Sled - ROV installed. Use on soft bottom. Mild scour tendency. 4-6 Amps output. (click here for more info) ![]() CP Mat - Combined stabilization mat and anode sled system. Use in any placement situation. High placement reliability for any seabed condition. 1-5 Amps output. (click here for more info) ![]() |
||
| Figure 2: Connectors that allow ROV or Diver to connect anodes to structures. RetroClamp - RetroClamp - Provides monitored connector between anode arrays and cathodically protected structures. (click here for more info) ![]() RetroPod - RetroPod tied to Jacket with RetroClamp for low cost platform retrofit. (click here for more info) ![]() RetroClamps - Pre-installed on anode sled (ExpandaSled) ![]() |
||
| Figure 3: Smart Anode Pod Structures SmartPod - Smart CP System for Deepwater pipelines, include pipe clamps and integral SunStation CP Monitor (click here for more info) ![]() SmartClamp - The new offshore CP solution for deepwater pipelines (RetroClamp and SunStation). (click here for more info) ![]() If you have any questions about this paper, or you would like to make an addition, please contact us. |
||

| deepwater corrosion services inc. | 10851 train court, houston, TX 77041, USA | +1 713 983 7117 | www.stoprust.com |