Piping Elbows

Piping Elbows and Bends are very important pipe fitting which are used very frequently for changing direction in piping system. Piping Elbow and Piping bend are not the same, even though sometimes these two terms are interchangeably used.A BEND is simply a generic term in piping for an “offset” – a change in direction of the piping. It signifies that there is a “bend” i.e,  a change in direction of the piping (usually for some specific reason) – but it lacks specific, engineering definition as to direction and degree. Bends are usually made by using a bending machine (hot bending and cold bending) on site and suited for a specific need. Use of bends are economic as it reduces number of expensive fittings.An ELBOW, on the other hand, is a specific, standard, engineered bend pre-fabricated as a spool piece  (based on ASME B 16.9) and designed to either be screwed, flanged, or welded to the piping it is associated with. An elbow can be 45 degree or 90 degree. There can also be custom-designed elbows, although most are catagorized as either “short radius” or long radius”.

In short “All bends are elbows but all elbows are not bend”

Whenever the term elbow is used, it must also carry the qualifiers of type (45 or 90 degree) and radius (short or long) – besides the nominal size

Elbows can change direction to any angle as per requirement. An elbow angle can be defined as the angle by which the flow direction deviates from its original flowing direction (See Fig.1 below).Even though An elbow angle can be anything greater than 0 but less or equal to 90°But still a change in direction greater than 90° at a single point is not desirable. Normally, a 45° and a 90° elbow combinedly used while making piping layouts for such situations.

piping elbow
Fig.1 A typical elbow with elbow angle (phi)

Elbow angle can be easily calculated using simple geometrical technique of mathematics. Lets give an example for you. Refer to Fig.2. Pipe direction is changing at point A with the help of an elbow and again the direction is changing at the point G using another elbow.

Fig.2 Example figure for elbow angle calculation
In order to find out the elbow angle at A, it is necessary to consider a plane which contains the arms of the elbow. If there had been no change in direction at point A, the pipe would have moved along line AD but pipe is moving along line AG. Plane AFGD contains lines AD and AG and elbow angle (phi) is marked which denotes the angle by which the flow is deviating from its original direction.
Considering right angle triangle AGD, tan(phi) = √( x2 + z2)/y
Similarly elbow angle at G is given by : tan (phi1)=√ (y2 +z2)/x
Elbow Radius:
 
Elbows or bends are available in various radii for a smooth change in direction which are expressed in terms of pipe nominal size expressed in inches. Elbows or bends are available in three radii,
a. Long radius elbows (Radius = 1.5D): used most frequently where there is a need to keep the frictional fluid pressure loss down to a minimum, there is ample space and volume to allow for a wider turn and generate less pressure drop.
b. Long radius elbows (Radius > 1.5D): Used sometimes for specific applications for transporting high viscous fluids likes slurry, low polymer etc. For radius more than 1.5D pipe bends are usually used and these can be made to any radius.However, 3D & 5D pipe bends are most commonly used
b. Short radius elbows (Radius = 1.0D): to be used only in locations where space does not permit use of long radies elbow and there is a need to reduce the cost of elbows. In jacketed piping the short radius elbow is used for the core pipe.
Here D is nominal pipe size in inches.
There are three major parameters which dictates the radius selection for elbow. Space availability, cost and pressure drop.
Pipe bends are preferred where pressure drop is of a major consideration.
Use of short radius elbows should be avoided as far as possible due to abrupt change in direction causing high pressure drop.
Minimum thickness requirement:
 
Whether an elbow or bend is used the minimum thickness requirement from code must be met. Code ASME B 31.3 provides equation for calculating minimum thickness required (t) in finished form for a given internal design pressure (P) as shown below:
bend thickness
Fig.3: Code equation for minimum thickness requirement calculation
Here,
R1 = bend radius of welding elbow or pipe bend
D = outside diameter of pipe
W = weld joint strength reduction factor
Y = coefficient from Code Table 304.1.1
S = stress value for material from Table A-1 at maximum temperature
E = quality factor from Table A-1A or A-1B
Add any corrosion, erosion, mechanical allowances with this calculated value to get the thickness required.
(source : http://www.whatispiping.com/piping-elbows-and-bends)

Pipeline Hot Tapping

Hot tapping, or pressure tapping, is the method of making a connection to existing piping or pressure vessels without the interruption of emptying that section of pipe or vessel. This means that a pipe or tank can continue to be in operation whilst maintenance or modifications are being done to it. The process is also used to drain off pressurised casing fluids.

Hot tapping is also the first procedure in line stopping, where a hole saw is used to make an opening in the pipe, so a line plugging head can be inserted.

Situations in which welding operations are prohibited on equipment which contains:

  • Mixtures of gases or vapours within their flammable range or which may become flammable as a result of heat input in welding operations.
  • Substances which may undergo reaction or decomposition leading to a dangerous increase in pressure, explosion or attack on metal. In this context, attention is drawn to the possibility that under certain combinations of concentration, temperature and pressure, acetylene, ethylene and other unsaturated hydrocarbons may decompose explosively, initiated by a welding hot spot.
  • Oxygen-enriched atmospheres in the presence of hydrocarbons which may be present either in the atmosphere or deposited on the inside surface of the equipment or pipe.
  • Compressed air in the presence of hydrocarbons which may be present either in the air or deposited on the inside surfaces of the equipment or pipe.
  • Gaseous mixtures in which the partial pressure of hydrogen exceeds 700 kPa gauge, except where evidence from tests has demonstrated that hot-tapping can be done safely.

Based on the above, welding on equipment or pipe which contains hazardous substances or conditions as listed below (even in small quantities) shall not be performed unless positive evidence has been obtained that welding/hot tapping can be applied safely

hottappinghottaaping2

(source : https://en.wikipedia.org/wiki/Hot_tapping)

Pipeline On-Bottom Stability Design

Pipeline laid on the sea floor should be stable during installation, after installation, and during operation. If the pipe is too light during installation, it will be hard to control the pipe since it behaves like a noodle due to waves & current and installation vessel’s motion. Most installation contractors require a minimum 1.15 pipe SG (specific gravity) to avoid pipe buckling which may occur due to pipe’s excessive movement during installation.

After installation, before the pipe is filled with water or product fluid, the pipe should be checked for 1 year return period waves and current conditions. If the pipe is laid as empty for a long period before commissioning, a 2-year, 5-year, or 10-year return period metocean data should be used. During operation, the pipe should be stable for a 100- year return period metocean data.

The soil data is very important to estimate the pipeline on-bottom stability. If no soil data is available, use the following data for the pipe-soil lateral friction coefficients per DnV RP-F 109, On Bottom Stability of Offshore Pipeline Systems:

  • Clay 0.2
  • Sand 0.6
  • Gravel 0.8

To keep the pipeline stable, the soil resistance should be greater than the hydrodynamic force induced on the pipeline.

onbottom1

μ is the soil friction coefficient as mentioned in the previous paragraph; Ws is the pipe submerged weight (lb/ft); ρw is the water mass density (64 lb/ft3); V is the near-bottom wave & current velocity; and A is the water particle acceleration corresponding to the V. The recommended lift, drag, and inertia force coefficient (CL, CD, and CM) is 0.9, 0.7, and 3.29 respectively.

The following methods (also see Figure 11.1) can be adopted to keep the pipeline stable on the sea floor:

  • Heavy (thick) wall pipe
  • Concrete weight coating
  • Trenching
  • Burial
  • Rock dumping (covering)
  • Concrete mattress or bitumen blanket
  • Concrete block

onbottom2

(Source : Introduction to Offshore Pipelines & Risers – Jaeyoung Lee (Page 83-85) )

Offshore Pipeline Installation

Offshore pipeline installation is the next step after designing. These days, there are few methods that commonly used and can be adapted to install offshore pipeline system, such as S-Lay method, J-Lay method, Reel Barge, and Beach Pull.

1.S-Lay Method

This method is quiet time-saving and can be done in vary depths. S-Lay refers to the pipeline shape forming “S” during the installation. This method requires lay-barge or other vessel designed to pipe-laying. Pipe is eased off the stern of the vessel as the boat moves forward. The pipe curves downward from the stern through the water until it reaches the seafloor. As more pipe is welded in the line and eased off the boat, the pipe forms the shape of an “S” in the water. Stingers, measuring up to 91 meters long, extend from the stern to support the pipe as it is moved into the water, as well as control the curvature of the installation. Some pipe-lay barges have adjustable stingers, which can be shortened or lengthened according to the water depth. In S-Lay method, pipe receive more stress, especially at the bending (curve). This may become a concern due to pipe-cracking.

instal1

Gamabr 1. S-Lay Method

2. J-Lay Method

J-Lay method put less stress on the pipe during installation, since there are only one bend (curve) forming the shape of “J”. This method inserts the pipeline in an almost vertical position. Pipe is lifted by a tall tower on the boat/barge, then inserted into the sea. The pipe bends once, under the water, taking on the shape of “J”.

instal2

Gambar 2. J-Lay Method

3. Reel Lay Method

This method is firstly proposed to install pipeline with relatively small in diameter. But it have been developed to install pipeline with 12″ to  16″ diameter in size. This method used coiled pipe on a spool (reel) resulting in fast productivity due to the ability to lay the pipe by “unwinding” it from the reel. The process costs due to the reduced number of personnel required to lay the pipe, lowering the risk of accidents at the same time, and providing efficiency in the availability of the pipe.

Each reel is designed to operate with a specific barge and can usually handle pipe from 2″ to 12″. The total length capacity depends on the spool dimensions and the diameter of the pipe.

instal3

Gambar 3. Reel-Lay Method

4. Beach Pull Method

Beach pull or also known as shore pull method is adapted for a near-shore pipe installation that is perpendicular to the shoreline, with pulling pipeline from the shore. Pipe is welded on a lay barge where the end of the pipe to shore set with pull head. Pull head hooks cable from shore.

The cable is connected to a winch on shore. Pulled pipe then glided into water through its route. Each segment of pipe is completed with buoy. When all pipes are on they’re position, buoys then being released.

(source : http://ifspipeline.blogspot.co.id/)

Bottom Roughness Analysis

Bottom roughness analysis adalah analisis yang diperlukan untuk mensimulasikan kondisi pipeline pada seabed apabila dipasang/di-laying, sehingga apabila terdapat free span atau titik sepanjang pipa yang beresiko mengalami stress/tegangan yang tinggi dapat diketahui sejak awal sehingga dapat direncanakan perbaikan kondisi seabed sebelum pipa dipasang (pre-lay correction) atau pun setelah pipa dipasang (post lay correction).

Pada analisis bottom roughness dibutuhkan data-data sebagai berikut.

  • Material dan penampang pipa (outer diameter dan wall thickness). Karakteristik ini diperlukan untuk mendefinisikan struktur (dalam hal ini pipeline) yang akan dilakukan analisis bottom roughness.
  • Properti pipa lainnya seperti isi pipa saat kondisi operasional, berat CWC (Concrete Weight Coating), serta temperatur pada saat kondisi operasional.
  • Profil dasar laut yang terdiri dari koordinat x-y relatif terhadap rute pipa yang akan ditinjau.
  • Kondisi tanah permukaan untuk menentukan tingkat penurunan muka tanah pada berbagai kondisi desain yang berbeda, misalnya instalasi, operasional, dan hydrotest.

Analisis bottom roughness akan menghasilkan output:

  • Plot tegangan pipa terhadap posisi rute pipeline
  • Plot posisi pipa vertikal pipa terhadap panjang pipa
  • Free span pada bentang pipa.

(Source : Tugas 2 Mata kuliah KL4220 Pipa Bawah Laut – Muhammad Deha Deni 15512072)

Pipeline Free Span Mitigation

During pipeline routing evaluation, consideration has to be given to the shortest pipeline length, environment conservation, and smooth sea bottom to avoid excessive free spanning of the pipeline. If the free span cannot be avoided due to rough sea bottom topography, the excessive free span length must be corrected.

Free spanning causes problems in both static and dynamic aspects. If the free span length is too long, the pipe will be over-stressed by the weight of the pipe plus its contents. The drag force due to near-bottom current also contributes to the static load. To mitigate the static span problem, mid-span supports, such as mechanical legs or sand-cement bags/mattresses, can be used.

Free spans are also subject to dynamic motions induced by current, which is referred to as a vortex induced vibration (VIV). The vibration starts when the vortex shedding frequency is close to the natural frequency of the pipe span. As the pipe natural frequency is increased, by reducing the span length, the VIV will be diminished and eliminated. Adding VIV suppression devices, such as strakes or hydrofoils, can also prevent the pipe from vibrating under certain conditions. The VIV is an issue even in the deepwater field since there exists severe near-bottom loop currents.

To prevent static and dynamic spanning problems, a number of offshore pipeline spanning mitigation methods in Table below have been identified. Based on soil conditions, water depth, and span

height from the seabed, the appropriate method should be selected. If the span off-bottom height is relatively low, say less than 1 m (3 ft), sand-cement bags or mattresses are recommended. If the span off-bottom height is greater than 1 m (3 ft), clamp-on supports with telescoping legs or auger screw legs are more practical. Graphical illustrations of each method are shown in Figure below.

Table and Figure about Free Span Mitigation Methods

freespan1freespan2freespan3

 

(Source : https://arifkl.wordpress.com/2013/02/03/free-span-mitigation/)

Analisis Tegangan Pipa

Perhitungan analisis tengangan pipa dilakukan untuk menjamin (to ensure) bahwa piping system tersebut dapat beroperasi dengan aman tanpa mengalami kecelakaan.

Dalam “kehidupannya”, piping yang didalamnya mengalir fluida, baik panas, dingin atau angat-angat kuku, akan mengalami pemuaian (expansion) atau pengkerutan (contraction) yang berakibat timbulnya gaya yang bereaksi pada ujung koneksi (connection), akibat dari temperature, berat pipa dan fluida itu sendiri serta tentu saja tekanan didalam pipa.

Dengan demikian, sebuah piping system haruslah didisain se-flexible mungkin demi menghindari pergerakan pipa (movement) akibat thermal expansion atau thermal contraction yang bisa menyebabkan:

  1. Kegagalan pada piping material karena terjadinya tegangan yang berlebihan atau overstress maupun fatigue.
  2. Terjadinya tegangan yang erlebihan pada pipe support atau titik tumpuan.
  3. Terjadinya kebocoran pada sambungan flanges maupun di Valves.
  4. Terjadi kerusakan material di Nozzle Equipment (Pump, Tank, Pressure Vessel, Heat Exchanger etc) akibat gaya dan moment yang berlebihan akibat expansion atau contraction pipa tadi.
  5. Resonansi akibat terjadi Vibration.

LOADINGS

Kita mengerti bahwa pipa menerima beban baik akibat berat pipa itu sendiri, berat fluida didalamnya, akibat tekanan dalam (internal pressure), temperature fluida, angin maupun gempa bumi atau earthquake.

Setiap beban yang diterima pipa akan ditahan oleh pipa tersebut sesuai dengan kemampuan dia menahannya, yang tentu saja tergantung dari material pipa yang kita gunakan.

Beban diatas dibagi dalam dua kelompok, yaitu:

1. Sustained Load:

yaitu beban akibat berat pipa, berat fluida, tekanan dalam pipa, tekanan luar, pengaruh angin dan gempa, serta beban dari salju yang menimpa pipa. Satu hal yang penting disini adalah jika pipa terkena beban demikian, maka bisa mengakibatkan pipa menjadi pecah dan collaps, jika tidak dilakukan upaya pencegahan.

2. Thermal Load:

beban ini adalah beban yang ditimbulkan akibat ditahannya expansion atau contraction suatu pipa yang mengalami pemuian ataupun pengkerutan akibat temperatur dari fluida yang mengalir didalamnya. Penahanan (restriction) yang diberikan dapat berupa Anchors, atau tersambung ke equipment. Satu hal yang perlu juga diperhatikan adalah bahwa thermal load ini adalah sifatnya siklus, artinya jika anchor nya dilepas atau fluidanya di hentikan mengalir di pipa tersebut, maka hilang pula load yang ditimbulkanya.

Kategori Teganggan (Stress)

  1. Primary Stress

Primary Stress adalah, sesuai namanya, Stress yang paling berbahaya yang diakibatkan oleh Sustained Load. Kenapa disebut berbahaya, karena jika timbul stress ini, maka efeknya catasthropic, yaitu rusaknya atau pecahnya pipa karena tidak mampu menahan berat atau beban yang ditimpakan kepadanya.

Primary Stress adalah direct stress, shear atau bending stresses yang dihasilkan oleh beban yang menimpa piping. Beban tersebut bisa datang dari pengaruh beban luar pipa seperti longitudinal dan circumferential stresses due to internal pressure dan bending dan torsional stresses karena berat pipa itu sendiri, snow, ice, wind atau earthquake. Sebagai tambahan akan ada bending dan torsional stress akibat dipasang Anchor atau jenis support lainnya yang juga menimpa pipa. Sehingga pipa diharapkan mampu menahan beban-beban tersebut dengan aman tanpa harus mengalami pecah atau gagal.

Tapi, jika ini terjadi ketika dilakukan perhitungan stress analysis dengan menggunakan program komputer, maka pemecahannya gampang sekali, yaitu dengan menempatkan tumpuan atau pipe support yang tepat pada lokasi yang overstress tadi, atau disekitarnya.

2. Secondary Stress

Secondary stress adalah stress yang diakibatkan oleh thermal loads. Yaitu akibat temperatur fluida yang mengalir yang menyebabkan pipa akan mengalami pemuaian atau pengkerutan (expansion or contraction).

Pipa akan menerima apa yang disebut bending nature yang bekerja pada penampang pipa (accross wall thickness) dan bervariasi dari negative ke positive dan timbul karena terjadinya beda defleksi secara radial dari pipe wall.

Secondary Stress bukanlah sebagai penyebab terjadinya kegagalan material secara langsung akibat beban tunggal. JIka pun terjadi stress yang melewati Yield Strenght, maka efek nya hanyalah terjadinya “local deformation” yang berkibat berkurangnya stress pada kondisi operasi.

Hanya sja jika hal ini berlangsung berulang-ulang, cyclic, maka akan timbullah apa yang disebut “local strain range” yang berpotensi menjadi penyebab timbunya Fatigue Failure.

3. ALLOWABLE STRESS

Untuk Primary Stress menggunakan Code Allowable STress pada Operating Temperature…(ASME B31.3 302.3.5 (c)

Karena Failure pada Secondary Stress adalah akibat terjadi gaya berulang pada pipa maka Allowable STress nya pun haruslah mempertimbangkan faktor siklus (cycles) yang diantisipasi akan terjadi sepanjang hidup pipa tersebut.

Kegagalan biasanya terjadi pada bagian yang mendapatkan regangan terbesar (highest cyclic strain).

Allowable Stress untuk Thermal Expansion Stress adalah:

SA = 1.25 Sc + 0.25 Sh

Sc = Allowable Stress pada temperature ambient
Sh = Allowable Stress pada temperature operasi

Allowable Stress ini akan menjadikan system piping akan aman beroperasi dalam siklus 7000 kali tanpa failure.

Jika siklus yang terjadi diharapkan lebih dari 7000 kali dalam umurnya pipa, maka Allowable Stress-nya akan berkurang dengan menambahkan faktor pada formula diatas.

SA = f(1.25 Sc + 0.25 Sh)….ASME B31.3 302.3.5 (1a)

Sc = Allowable Stress pada temperature ambient
Sh = Allowable Stress pada temperature operasi
f= Stress Range Factor, dari figure 302.3.5 ASME B31.3.

(Sumber : https://syae007.wordpress.com/2010/01/20/pengantar-pipe-stress-analysis/)

PIPELINE MAINTENANCE: Magnetic Leakage Detection Used to Spot and Measure Pipeline Cracks

3-1

A standard axial configuration high-resolution inspection vehicle

Magnetic flux leakage (MFL) inspection is the most commonly used tech-nology for the inspection of in-service pressurized pipelines. It is estimated that about 80% of line inspection missions are carried out using this technique. The technique is robust and reliable, and advances over the last 25 years have resulted in high resolution inspection systems that achieve accurate and repeatable measurement of defects in the pipeline. High quality inspection can be achieved with minimal disruption to daily operations.

The traditional use of MFL technology has been the detection and measurement of metal loss defects, primarily corrosion, and this is the inspection mission for which the technology is best known. What is less well known is that high resolution MFL technology can be used and adapted for the location and measurement of cracks in the pipeline, in circumferential and longitudinal directions.

Principles of inspection

The basic physics of the technique are very well known. The pipe-wall is magnetized axially by a pair of magnet and bristle rings at each end of the magnetizer vehicle. Any disruption to the flow of magnetic field in the pipeline steel, as caused by metal loss in the wall, will cause disruption to and leakage of the field. It is this leakage that is detected and measured by the sensors on board the inspection vehicle.

The axial configuration was initially chosen as the most practical engineering solution and because this configuration enabled the inspection vendor to detect and measure those defects that most commonly occurred in pipelines and were of the most concern to pipeline operators. There are some shortcomings in this technique when looking for defects that have a more longitudinal component. These shortcomings can be addressed by altering the magnetic configuration of the inspection vehicle.

Circumferential Cracking

3-2

A standard grey scale output of inspection data from the Pll tool. The girth weld can be seen in the center of the plot

The most common form of circumferentially aligned crack-like defect occurs within the girth weld. Girth weld defects, introduced during construction, can include incomplete weld passes, stop-start, unauthorized weld repairs, and cracking caused by inadequate heat treatment of the weld area.

As these defects are circumferentially aligned, and therefore at right angles to the flow of magnetic flux, they can cause a disruption and leakage of the field that is readily detected. However, the fact that these defects by their very nature are within a girth weld, poses significant technical challenges.

The girth weld itself presents a barrier to axial flux flow, causing a large disturbance to the signal, which can mask defects within the weld. In addition, and perhaps more significantly, the protrusion of the weld bead into the pipeline bore can cause the MFL sensors to “lift off” the inside of the pipe wall.

If the vehicle is traveling at normal pipeline speeds and the sensor design has high inertia, then a dead zone can be created both at the girth weld and for some distance downstream of the girth weld. This means that inspection vehicles cannot detect defects within the girth weld, and indeed for some distance beyond it. In some cases, this non inspected dead zone can be as much as 200 mm.

When a high resolution inspection vehicle was first developed by PII in the mid-1970s, these shortcomings in available technologies were recognized. The initial specification of the vehicle performance required that 100% of the pipeline be reliably inspected, including the girth weld and the area around it. So care was taken at the very start of the project to ensure that full inspection capability was not compromised by the presence of the girth weld.

The first problem, that of the large and sometimes confused signal generated by the weld, was tackled by using the very high magnetic field of the PII tool (necessary to saturate the pipe wall and generate repeatable signals from small defects). This, coupled with the very high sensor density of the high-resolution tool, means that the signal from normal girth welds is remarkably repeatable, and any abnormality in the weld can be easily identified.

Designing the sensor heads themselves to have very low mass solved the more serious problem of sensor lift-off. This design, coupled with very light spring suspension, means that the sensor carrier has low inertia and ‘bends’ with the weld bead, traveling over it smoothly rather than bouncing off the pipe wall.

The fact that all girth weld anomalies are by definition very short in the axial direction can pose problems for the analyst. It can be difficult to discriminate between the various types of defects that can occur in girth welds. The solution lies in the experience and training of data analysts. The first girth weld crack was identified and confirmed in the early 1980s. Since that time, we have located and confirmed more than 1,000 girth weld cracks in operational pipelines.

Longitudinal Cracking

3-3

A further example of NAEC ilustrates the view achieved by this technique

The extent of the flux leakage created by a pipe wall anomaly, and therefore the size of the signal collected by the in-line inspection device, is affected by the width of the anomaly. A circumferentially wide defect will set up greater opposition to the flux induced by the tool, and a larger signal will result.

The reverse also holds true. As a longitudinally aligned defect becomes narrower, its opposition to flux flow diminishes, and the resultant signal will decrease in magnitude. The extreme of this phenomenon is demonstrated by the fact that longitudinally aligned cracks cannot be detected using conventional magnetic flux leakage technology.

The result is that with inspection devices carrying only a few MFL sensors, a longitudinally aligned defect will not be detected. With high-resolution tools the high sensor density enables the defect to be detected, but the reduction of the signal strength can lead to an underestimation of the size of the defect.

The defects that have been recognized as present in some pipelines and designated as narrow axial external corrosion (NAEC) are very rare in PII’s experience, as they are not only narrow but are longitudinally orientated, axially long and relatively smooth in profile.

Following the discovery of NAEC on one particular pipeline, the data from the previous MFL inspections of that line was examined closely by a PII-client team. Although it was confirmed that the inspection tool had collected data from these defects, the level of signal was such that the depth of the NAEC had indeed been underestimated.

An attempt was made to create algorithms that would recognize the character of NAEC, and correct the sizing model to compensate for the problem and predict depth more accurately. This project met with some limited success, but was found not to be 100% reliable for the purpose of establishing confidence in the condition of the pipeline, given the extent of the NAEC phenomenon.

Transverse Field Inspection

3-4

Sample of the Transcan data are shown alongside sections of the actual defects that were excavated and removed from the pipeline

If metal loss that is long and narrow will not produce signal strengths compatible with accurate sizing when the magnetic field is longitudinal, then another approach is to magnetize the defect in the orthogonal direction. This means that a tool had to be devised and constructed that would magnetize the pipe in the circumferential direction.

Theoretically, this means that the signal obtained will be far more prominent and will allow more accurate characterization. In addition, the axial extent of the defect should be clearer.

The idea of applying the magnetic field in the transverse direction is not new. AMF (formerly American Machine and Foundry) was probably the first to develop the idea as part of their mill inspection technology in the 1960-1970 period and patented a rotating transverse field system in 1978.

PII also examined it.

The reason these designs and prototypes never came to fruition was due to a limitation of the technology available at the time, rather than in the technique itself. Data in the 1970s was usually stored on reel-to-reel recorders, and displayed on UV sensitive paper. Given the advances in computing techniques, materials science, and electronics since then, confidence that a solution for the problem of long narrow defects could be achieved was high. However, without a commercial impetus, the technique was probably destined for obscurity. The discovery of NAEC and several long seam defect failures in North America provided the impetus to develop a commercially viable inspection system. A prototype, dubbed the Transcan tool was designed, constructed, and launched within a five week period and collected good quality data on its first inspection run of more than 200 km.

Analysis of the data and subsequent excavation revealed that the tool did provide an improved characterization of NAEC. This was particularly promising when considering that both the tool and the analysis technique were first attempts. The short times cales available for right-of-way access meant that only a limited amount of information could be gathered from field excavations, but the wealth of data obtained from the excavations carried out in 1996 means that extensive detailed correlation is possible.

Hook cracking

Encouraged by this success, PII refined the process still further to build an in-line inspection tool that would reliably detect and characterize long seam defects. This work was encouraged by one client who had experienced operational failures caused by hook-cracking in a 20-in. crude oil pipeline.

Defects, such as hook cracks and lack of fusion, have caused many in-service and hydrotest failures, especially in liquid lines subject to pressure cycling. Hook cracks occur when inclusions at the plate edge are turned out of the plane of the steel during the pipe manufacturing and welding process. These may pass the initial hydrotest, but fail later through fatigue-induced cracking. It is the turning out of the metal at the weld which gives the crack its characteristic “hook” or “J” shaped appearance.

Although such defects can be det-ected by manual non-destructive testing (NDT) methods, they have remained largely outside the domain of automated methods and in-line tools, which are used for the mass inspection of pipelines. Until recently, the only option was to hydrotest the line. This has limitations in as much as it gives an “all or nothing” or “yes/no” indication. It is not a quantitative technique.

Severe defects are identified through failure, but no information is conveyed about less significant defects which may themselves grow to criticality within a short time after the test. To ensure these defects are found, repeated testing at frequent intervals is required. In addition, following a hydrotest where there has been a failure, the line must be repaired and hydrotested repeatedly until there are no more failures. This is costly in terms of effort and lost throughput.

In this case, the service failures experienced in this 1500-km-long, 20-in. pipeline had resulted in a significant reduction in throughput for the pipeline, with subsequent loss in revenue, and a regulatory requirement to hydrotest the entire pipeline, at a projected cost of tens of millions of dollars.

In the spring of 1998, PII developed a high-resolution 20-in. Transcan tool carrying 400 primary sensors, which was laboratory tested and used to inspect 140 miles of 20-in. pipeline. The tool was successful. In order to validate the technology, the client excavated the reported defects and repaired and hyrotested the line. Two separate sections of the line, totaling 118 miles, were hydrotested to 125% MOP without failures.

More than 50 hook-cracks were detected by the tool and validated by “in the ditch” NDE. The smallest was 5-10% of pipe-wall thickness (Fig 11 and 12). In addition, many examples of lack of fusion and stitching, and three examples of cracks within dents were detected. Only two of the cracks verified would have failed a hydrotest at 125% MOP. The hydrotest requirement was lifted and following the inspection and repair of the remainder of the 1500-km line, full operating pressure was restored.

During the course of the remaining inspection, many hundreds of long-seam defects were revealed and repaired.

The Transcan has been used to inspect over 4,000 km of pipeline, and plans are to extend the range up to 42 in. and down to 8-in., with a 6-in. tool being a distinct possibility in the future.

Stress corrosion cracking

Given its sensitivity to axial features, would TFI be able to detect stress corrosion cracking? Recent work on behalf of the operator of a refined products line has shown some initial promise. Specifications of the line are seamless, 12-in. in diameter, 100 km in length, wall thickness of 6.35-7 mm X52 & X60 grade steel, and is 30 years old.

The pipeline had suffered from several failures due to stress corrosion cracking (SCC) and regulatory authorities required that the operating pressure be reduced from 90 bar to 60 bar and a program of hydrotesting be implemented. To investigate the capability of detecting SCC, a test program was undertaken on samples of defective pipe.

In parallel, a 12-in TFI tool was prepared for a trial run in the pipeline. The results from this run have been analyzed, and reporting will be followed up by proving excavations. The laboratory tests showed that it was possible to observe some colonies of SCC using the Transcan technique. However, as always, the true test is in the ability to discriminate these signals from other features in the line, such as manufacturing variations, corrosion sites, surface roughness, etc.

In parallel with this investigative inspection program, extensive testing was carried out on the Transcan tool using known colonies of SCC installed in a pull through string. TFI is not intended to be a primary inspection tool for SCC (ultrasonic tools probably offer the best performance here), but any success in this area is regarded as a bonus on top of its capability at inspection for axial metal loss features and defects in long seam welds.

Third party damage

During the inspection and subsequent repair of the 20-in. pipeline described previously, several instances of third party damage were located and confirmed. – Shown is an instance of third party damage uncovered on this pipeline.

As third party damage is the largest cause of pipeline failure in most countries, we feel that the technology has potential to allow pipeline operators to not only detect, but also characterize these kinds of defects. A development program has begun in the US with the Battelle Institute, the Gas Research Institute, and the Office of Pipeline Safety. This program should allow the development of a system for accurate location, identification, and characterization of this difficult-to-detect defect.

Crack-like defects in operating pipelines have long been the most difficult defect to locate using in-line inspection techniques. For many years, the pipeline industry has had to rely on the inexact science of hydrotesting to mitigate risk from failure due to cracking. New tools are superior to hydrotesting, technically and financially. ;

Acknowlegement

A slightly longer version with more illustrations was presented at the PII 5th Annual Pipeline and Pigging conference in Seville, Spain.

(Source : http://www.offshore-mag.com/articles/print/volume-60/issue-11/news/pipeline-maintenance-magnetic-leakage-detection-used-to-spot-measure-pipeline-cracks.html)

Pemilihan Rute Pipa Bawah Laut

rute pipa bawah laut

Tampak rute pipa bawah laut

(sumber : http://subseaworldnews.com )

1. Jalur yang terpendek

Idealnya berupa garis lurus, semakin pendek jalur pipa yang digunakan maka akan meminimalisasi penggunaan material hingga barge ataupun laying vessel. Selain itu, pemilihan jalur yang terpendek juga akan meminimalisasi penggunaan biaya yang dikeluarkan. Dan juga akan mengurangi efek head loss akibat gesekan fluida denga permukaan dalam pipa, akibat belokan, dan sebagainya.

2. Jalur yang paling mudah untuk diinstalasi

Kondisi batimetri atau permukaan dasar laut sangat berpengaruh dalam proses instalasi. Semakin tidak rata suatu permukaan dasar laut maka semakin susah proses instalasi pipa untuk dilakukan. Selain itu untuk kondisi permukaan yang tidak rata tersebut perlu keakuuratan tinggi untuk meletakkan pipa pada rute yang telah ditentukan. Selain itu juga diperlukan koreksi-koreksi baik pre-lay ataupun post-lay.

3. Jalur yang paling aman

Tingkat keamanan jalur sangat bergantung pada kondisi batimetri, dasar laut yang relatif rata merupakan pilihan jalur untuk pipeline yang aman karena mengurangi resiko akibat free span dan VIV (Vortex-Induced Vibration).

4. Jalur yang menggunakan biaya paling sedikit (paling murah)

Semakin sedikit biaya yang dikeluarkan maka semakin baik, untuk meminimalisasi biaya dapat dilakukan dengan cara mencari jalur terpendek sehingga pipa yang digunakan lebih sedikit, maka pengeluaran untuk pengadaan pipa pun lebih sedikit. Selain itu juga bisa dengan mencari instalasi yang paling mudah. Dengan instalasi yang mudah maka peralatan-peralatan yang digunakan pun dapat di minimalisasi sehingga juga mengurangi biaya pengeluaran.

(Sumber : Slide 02 KL 4220 Pipa Bawa Laut, Prof. Ir. Ricky Lukman Tawekal, MSE, PhD dan Eko Charnius Ilman, ST, MT)