THE APPLICATION OF LONG RANGE GUIDED ULTRASONICS FOR THE INSPECTION OF RISER PIPES

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THE APPLICATION OF LONG RANGE GUIDED ULTRASONICS FOR THE INSPECTION OF RISER PIPES J. McGregor, B. Nooteboom, N. Ivory PTAS-ITS Lot 1 and 2 Tapak Perindustrian Pekan Belait, Jalan Setia Di-Raja, Kuala Belait, Brunei Darussalam Abstract: Corrosion and other defects that reduce the cross-sectional area of pipes cause major problems in the oil, chemical and the other industries. Most standard NDT methods measure the remaining pipe wall accurately, but over a small area so it is almost always uneconomic to inspect 100% of the pipe. In practice a pragmatic approach is usually adopted where the wall thickness at a number of points is measured and this information is used to determine the fitness for purpose of the pipe. However, this approach generally requires unrestricted access to the outer surface of the pipe and this is not possible, if the pipe is insulated, has protective coatings or is buried. This means that even external corrosion cannot be seen so that accurate measurements of the remaining wall can be made at the correct location on the pipe. Ultrasonic guided wave inspection using the Wavemaker Pipe Screening System (WPSS) offers a novel solution to many such inspection problems. Guided waves can be excited from easy to access locations on the pipe and will propagate many metres along the pipe, the returning echoes indicating the presence of corrosion or other pipe features. PTAS-ITS now use the WPSS routinely in Brunei and Indonesia; this paper discusses our operational experience in proving the technique to our client and presents recent inspection results on riser pipes inspected in Indonesia. Introduction:This paper discusses our operational experience in proving the technique to our client and presents recent inspection results on riser pipes inspected in Indonesia. 1 The application of long range guided ultrasonic waves for the inspection of riser pipes Long Range Guided Ultrasonics Guided Ultrasonics makes the Wavemaker pipe screening system. It is important to understand from the beginning that this is a screening tool. It is not a magic solution to all inspection problems. What is does do is provide a method of rapidly determining where there are problem areas on a pipe. Wavemaker Pipe Screening System 2 What is Long Range UT (LRUT)? In LRUT an array of ultrasonic transducer elements are fitted around the pipe. Instead of scanning the region directly below or near to the transducers, guided waves travel down the length of the pipe. This allows 10's of meters to be inspected from a single location. In this picture you can see a ring attached to a section of EPDM wrapped 30 diameter pipe. From this single location low frequency guided waves are transmitted in both directions along the length of the pipe screening difficult to access areas remotely. Page 2 What is long range UT : Instead of scanning the region directly below or near to the transducers, guided waves travel down the length of the pipe. This allows 10's of meters to be inspected from a single location. In this picture you can see a ring attached to a section of EPDM wrapped pipe. From this single location waves are sent in each direction.

12.0 10.0 8.0 6.0 4.0 2.0 0.0 0.0 5.0 10.0 15.0 20.0 3 How Does It Work? To perform the test, a ring is placed around the pipe. No couplant is needed as the transducers dry couple on to the pipe. The surface of the pipe does not usually need to be prepared. Any loose flaking paint or corrosion needs to be scraped off of the pipe, but otherwise, no preparation is necessary. The technique works by looking for reflections from changes in cross section of the pipe. These reflections are collected and analysed. Potential problem areas are identified and can be investigated using another technique to determine area and severity. In this picture the area of test is the straight piece of pipe after the bend under the EPDM wrap Page 3 To actually perform the test, a ring of transducers is placed around the pipe. No couplant is needed. The transducers dry couple on to the pipe. The surface of the pipe usually does not need to be prepared. Any loose flaking paint or corrosion needs to be scraped off of the pipe, but otherwise, no preparation is necessary. In this picture the area of test is the straight piece of pipe after the bend under the EPDM wrap. 4 What Can It do? Can be performed without taking the pipe out of service Can be performed at elevated temperatures up to 120 C Can be performed under coatings, Ground, Concrete, Cladding, Bitumen, Ethylene Propylene Diene Momomer (EPDM) etc It is sensitive to corrosion anywhere on the circumference of the pipe It is equally sensitive to both internal and external corrosion The entire volume of the pipe is inspected (within the diagnostic length of a test). Not only spot locations Pulse echo type operation provides information on feature position and approximate size Sophisticated analysis aids interpretation of results Page 4 The inspection can be performed without taking the pipe out of service. The entire volume of the pipe is inspected. It does not sample at only spot locations, it is sensitive to corrosion anywhere on the circumference. It is equally sensitive to both internal and external corrosion. The technique works by looking for reflections from changes in cross section of the pipe. Long ranges of pipe can be screened from a single location. 5 Amp (mv) Clean Pipe Factors affecting the results: General Condition of Pipe Distance (m) Generally Corroded Pipe The propagating guided waves reflect from all changes in cross section no matter how small. The reflections from small amounts of corrosion appear as a 'noise' floor on the trace. For example in the trace above, the pipe section on the left is a clean pipe, but the section on the left is generally corroded like the pipe shown on the bottom right. Page 5 The propagating guided waves reflect from all changes in cross section. The reflections from small amounts of corrosion appear as a 'noise' floor on the trace. For example in the trace above, the pipe section on the left is a clean pipe, but the section on the left is generally corroded like the pipe shown on the bottom right. 6 Factors affecting the results: Type of defect More difficult Single isolated pit Smooth gradual defects Axial cracks Small pits in welds Easier A cluster of pits Sharp corrosion Circumferential cracks Large cracks in welds Factors affecting the results Type of defect. Page 6

7 Amp (mv) 0.6 0.4 0.2 0.0 -F3 -F2 -F1-20 -10 0 10 20 Distance (m) Exposed side shows little attenuation Factors affecting the results: Effect of Wrapping +F1 Strong attenuation is caused by wrapping Another factor that strongly affects the results is the type of wrapping that surrounds the pipe. Many wrappings can cause some attenuation. Bitumen causes a very high amount of attenuation as can be seen in the result above. The guided wave can easily propagate in the non-wrapped side on the left of trace shown above. However, the wave quickly dies away in the bitumen wrapped section. In general, only the first few meters of a bitumen wrapped section of pipe can be inspected. These first few meters are usually the most likely to corrode Page 7 The type of wrapping that surrounds the pipe strongly affects the results. Bitumen causes a very high amount of attentuation as can be seen in the result above. The guided wave can easily propagate in the nonwrapped side. However, the wave quickly dies away in the bitumen wrapped section. Usually only the first few meters of a bitumen wrapped section can be inspected. These first few meters are usually the most likely to corrode. 8 Typical Ranges (in each direction, using standard transducers) The range that can be inspected in a single test varies greatly depending on such items as the condition of the pipe and any coatings that have been applied. The list below shows some typical ranges that can be expected when the standard transducer configuration is used. Ideal conditions 80m (160 metres in total test length) Typical 30 year old pipe with little internal or external corrosion 40m (80 metres in total test length) Typical 30 year old pipe with some general corrosion 20m (40 metres in total test length) Typical pipe wrapped in factory applied foam 15m (30 metres in total test length) Heavily corroded pipe or pipe that is bitumen wrapped 5m (10 metres in total test length) Six welds (Each direction) The first flange or the second bend or branch Note: these ranges can be doubled by using low frequency transducers Page 8 The range that will be inspected in a single test varies greatly depending on such items as the condition of the pipe and any coatings that have been applied. The slide above shows some typical ranges that can be expected when the standard transducer configuration is used. If the low frequency transducers are used, these ranges can normally be doubled (or more). 9 What Are The Benefits? Access is not required to the area requiring inspection Ability to test metres of pipe at a time Usually no surface preparation required Difficult to inspect areas such as insulated or buried sections of pipe can be screened for defects No access to Area of test Access is not required to the area requiring inspection, it has the ability to test many metres of the riser at one time. Usually no surface preparation is required. Difficult to inspect areas such as splash zone or buried sections of the riser can be inspected. Page 9 10 What Are The Limitations? Best employed as a screening tool to identify troubled areas Does not give finite sizes Cannot resolve small pits Cannot differentiate between internal and external corrosion LRUT can be best employed as a screening tool that is used to identify trouble areas. Once these trouble areas have been identified they can be targeted using other methods of examination. This allows for 100 percent coverage at a fraction of the price of many other methods. 8 Ring R2F8 Page 10

11 What was the job? Ring position Test area Page 11 This slide is typical of the working conditions; this is in the tidal zone of a river estuary. For larger diameter pipes, an inflatable belt system is used. The system allows for a light flexible application of the technique to large diameter pipes. The normal range of inflatable rings is from 6 to 24 inches in diameter. (Larger pipes can be inspected, but on large pipes only large corrosion patches can be found.) 12 Client Requirements Our client, a major international oil producer, had a corrosion problem on a gas riser resulting in an explosion. The problem was related to external corrosion on the riser in the tidal zone interface. Their requirement was to carry out non intrusive inspection on the risers without removing corrosion product, excavating or shutting down the line to determine whether corrosion was present in the tidal area and give an estimate of its size. The work was to be carried out in conjunction with a maintenance programme on the risers. The risers were first tested by LRUT to determine the extent of corrosion present and only then were the maintenance crew able to disturb remaining surface corrosion for repair purposes. The work was to be carried out in conjunction with a maintenance programme on the risers. The risers were first tested by LRUT then only were the maintenance crew able to disturb remaining surface coatings for repair purposes. Page 12 13 Description of Work The work scope consisted of carrying out Long Range UT on 13 off risers ranging from 6 to 30 diameter without disrupting ongoing repair work or affecting production. This slide shows another typical location of the worksite. The job entailed carrying out LRUT on 13 risers from 6 to 30 inch diameter in the splash and ground entrance area. Page 13 14 The problems Site : Location of work was in a tidal range of a river delta. Risers : Ranged in size from 6 to 30 diameter Access : Access was restricted on some risers to locations that did not provide for the best test parameters. Timing : Timing was restricted in some locations as the risers were situated on the tidal flats. Coatings : Riser coatings consisted of up to 12mm thick EPDM coating and or epoxy polyproplyene covering the tidal zone area. Proving : We had to prove to the clients satisfaction that the system was capable of detecting the size and type of corrosion he was interested in. The Client was interested in detecting corrosion equivalent to 5 % change in cross sectional area. Page 14

15 Our client was concerned that the guided waves would not be able to penetrate the EPDM coating to the area of interest, which was the tidal zone of the riser. This area could be up to 8 metres away from the start of the wrapping. We had to prove to the client that the system had the capability to detect a 5% loss of CSA defect as far away as possible from the ring location. Proving the system Concrete coating EPDM coating Page 15 Our client was concerned that the guided waves would not be able to penetrate the EPDM coating to the area of interest, which was the tidal zone of the riser. This area could be up to 8 metres away from the start of the wrapping. We had to prove to the client that the system had the capability to detect a 5% loss of CSA defect as far away as possible from the ring location. 16 A 20 diameter by 25.4mm thick test riser was made available for proving the technique. This riser had 12metres of EPDM coating on the pipe and 3.1metres of epoxy fiberglass coating on the bend. The Test Riser We were supplied with a redundant test riser to prove the system to the client. We were able to introduce artificial defects into the riser at various locations. The object of the testing was to determine if a 5% loss of cross sectional area on the elbow could be reliably detected through the coating from the other end of the pipe. Page 16 17 The Defects 4 defects were introduced into the riser at a a variety of locations 1:100mm x 300mm x 11mm deep = 9% change in CSA 2:100mm x 300mm x 11mm deep = 9% change in CSA 3:50mm x 300mm x 11mm deep = 9% change in CSA 4:100mm x 100mm x 6mm deep = 2% change in CSA 4 defects were introduced by grinding, ranging from 2% to 9% change in CSA. Open pipe end, 300mm clear of coating Defect 1, 5m from pipe end Defect 2, 9.2m from pipe end Defect 3 adjacent to weld Weld, 200mm from EPDM 5.0 metres 4.2 metres 3.0 metres 3.0 metres Defect 4, 1.7metres from weld 45 deg, 5d elbow Polypropylene coated Page 17 18 Scanning the Riser Testing using standard frequency transducers at 35mm spacing resulted in better than expected results. The best results were obtained from a frequency of approximately 26 to 30kHz and an excitation signal of 8 to 10 cycles Hanning. This resulted in the reliable detection of an artificial defect in the outside of the elbow 100mm square by 6mm deep equating to a 2% loss of cross sectional area, from a location 13 metres away, through an EPDM coating length of 11.5m and 1.5m of Epoxy fibreglass. The next slide shows the results achieved from the location at defect 1 Defect 4 Page 18 The riser was scanned from a variety of locations whilst the defects were being introduced utilising both low frequency and standard probes. The testing was stopped when we were able to prove to the client that we were able to consistently record defect 4 located in the outside of the elbow and equivalent to a change in CSA to 2% through more than 11metres of EPDM coating.

19 Standard frequency scan Reverberations This slide shows the results of one of the final scans. The location of test is adjacent to defect 1. All the other defects can be clearly seen even defect 4 which is equivalent to a 2% change in CSA and defect 3 which is only 50mm to a weld. Defect 2 Defect 3 can be resolved Defect 4 Page 19 20 Close up of defect 3 and weld Defect 3 was introduced into the pipe adjacent to a weld (within 50mm) in order to determine whether it could be detected. Using the higher frequency transducers and a hanning tone burst, this defect is able to be resolved. This slide shows the resolution of the system, as the defect can be detected, but the sizing is not as accurate as if the defect was further away. Defect 3 Weld Defect 3 was introduced into the pipe adjacent to a weld (within 50mm) in order to determine whether it could be detected. This slide shows the resolution of the system, as the defect can be resolved but the sizing is not as accurate as if the defect was further away. Page 20 21 The test risers A risk analysis carried out by the client revealed 13 risers which required urgent inspection. These risers ranged from 6 to 30 diameter, of which 10 were found to have reportable corrosion of above 10% loss of cross sectional area. One was determined to have more than 50% loss of CSA. The following slides detail a selection of these tests. A risk analysis carried out by the client revealed 13 risers, which required urgent inspection. Page 21 22 8 riser location This riser was located offshore, in shallow water. Page 22

23 8 riser details This riser was 8 diameter by 20mm thick. It was located on an offshore installation in shallow water. The coating consisted of EPDM wrap. No significant corrosion was detected within a 14m test range This section is included as a comparison between a riser in good condition compared to the following 1 in poor condition. Page 23 24 This scan shows clean pipe with no significant corrosion present. The double echos at positions 3 and 4 are due to the difference in distance between the inside and outside radius of the swept bends from the ring position. 8 riser report The scan shows clean pipe with no significant corrosion present. The double echos at positions 3 and 4 are due to the difference in distance between the inside and outside radius of the swept bends from the ring position. Page 24 25 6 riser location This slide shows the ring location and the vertical section of the riser. Coating breakdown and corrosion Page 25 26 6 riser details This riser was 6 diameter by 18mm thick. It was located on an offshore installation in shallow water. The bitumen type coating was severely broken down in the splash zone area. External corrosion could be seen visually on this riser but due to the heavy corrosion products the remaining thickness could not be assessed. Corrosion was detected up to 50% wall loss within a 10 metre test range. This test range was limited by the extent and severity of the corrosion present. Page 26 This riser was 6 diameter by 18mm thick. It was located on an offshore installation. The bitumen type coating was severely broken down in the splash zone area. Corrosion was detected up to 50% wall loss within a 10 metre test range. This test range was limited by the extent and severity of the corrosion present.

27. 6 riser drawing 400mm 500mm Shows a drawing of the layout of the riser with corrosion detected beyond the lower riser bend. 500mm 2750mm 1200mm!!!!!!!! 150mm 950mm 1100mm Sea level 400mm Ring Position! Severe corrosion above 50% loss of CSA! Medium corrosion 20% to 50% Sea bed los s of CS A Page 27 28 This scan shows the extent of the corrosion. There is lots of red and black together. It shows a lot of general corrosion, This was backed up with manual UT where possible. 6 riser results This scan shows the extent of the corrosion. There is lots of red and black together. It shows a lot of general corrosion, which was backed up with manual UT carried out by a diver. A good correlation was achieved between the results of the LRUT and the manual scanning. Page 28 29 30 riser location This slide shows another 30 riser location. We are shooting towards the ground from this ring location. It is typical of the working conditions in this area and is located at a river crossing and had a combination of coatings, Bitumen where it entered the ground and EPDM/Concrete where it entered the water. Page 29 30 Conclusion Long range UT has proven to be a useful tool in the inspection of offshore risers, enabling the pipeline reliability engineers to predict remaining life span and direct maintenance costs, where appropriate, without the requirement for costly pipeline shutdown and pigging operations. Long range UT has proven to be a useful tool in the inspection of offshore risers enabling the pipeline reliability engineers to predict remaining lifespan and direct maintenance costs, where appropriate, without the requirement for costly shutdown or pigging operations. Page 33