preparation of pipeline

preparation of pipeline



5.1.1 Stringing
At steel rolling mills where the pipe is fabricated, pipeline representatives will carefully inspect new pipe to assure that it meets industry and federal government safety standards. For corrosion control, the outside surface will be treated with a protective coating.
The pipe will be transported from the pipe mill to a pipe storage yard in the vicinity of the pipeline location. The pipe lengths typically are 40 to 80 feet long. A stringing crew using specialized trailers will move the pipe from the storage yard to the pipeline right-of-way. The crew will be careful to distribute the various pipe joints according to the design plan since the type of coating and wall thickness can vary based on soil conditions and location.


Fig(5-1) Stringing Process

For example, concrete coating may be used under streams and wetlands, and heavier wall pipe is required at road crossings and in special construction areas.


5.1.2 Trenching
The trenching crew will use a wheel trencher or backhoe to dig the pipe trench. The U.S. Department of Transportation (DOT) requires the top of the pipe to be buried a minimum of 30 inches below the ground surface in rural areas, so the depth of the trench will be at least five to six feet deep for pipe 30 to 36 inches in diameter. For less rural areas, the pipe must be buried a minimum of 36 inches. The pipe will be buried even deeper at stream and road crossings.


Fig (5-2) Trenching Process

If the crew finds large quantities of solid rock during the trenching operation, it will use special equipment or explosives to remove the rock. The contractor will use explosives carefully, in accordance with state and federal guidelines, to ensure a safe and controlled blast.

In cultivated areas the topsoil over the trench will be removed first and kept separate from the excavated subsoil, a process called top soiling. As backfilling operations begin, the soil will be returned to the trench in reverse order with the subsoil put back first, followed by the topsoil. This process ensures the topsoil is returned to its original position.

5.1.3Pipe Bending

The pipe bending crew will use a bending machine to make slight bends in the pipe to account for changes in the pipeline route and to conform to the topography.
The bending machine uses a series of clamps and hydraulic pressure to make a very smooth, controlled bend in the pipe. All bending is performed in strict accordance with federally prescribed standards to ensure integrity of the bend.


Fig (5-3) pipe bending Process

5.1.4 Welding

The pipe gang and a welding crew will be responsible for welding, the process that joins the various sections of pipe together into one continuous length. The pipe gang uses special pipeline equipment called side booms to pick up each joint of pipe, align it with the previous joint and make the first part (pass) of the weld. The pipe gang then moves down the line to the next section repeating the process. The welding crew follows the pipe gang to complete each weld.
In recent years, contractors have used semi-automatic welding units to move down a pipeline and complete the welding process. Semi-automatic welding, done to strict specifications, still requires qualified welders, and personnel are required to set up the equipment and hand-weld at connection points and crossings.
As part of the quality-assurance process, each welder must pass qualification tests to work on a particular pipeline job, and each weld procedure must be approved for use on that job in accordance with federally adopted welding standards. Welder qualification takes place before the project begins. Each welder must complete several welds using the same type of pipe as that to be used in the project. The welds are then evaluated by placing the welded material in a machine and measuring the force required to pull the weld apart. It is interesting to note that the weld has a greater tensile strength than the pipe itself.

A second quality-assurance test ensures the quality of the ongoing welding operation. To do this, qualified technicians take X-rays of the pipe welds to ensure the completed welds meet federally prescribed quality standards. The X-ray technician processes the film in a small, portable darkroom at the site. If the technician detects any flaws, the weld is repaired or cut out, and a new weld is made. Another form of weld quality inspection employs ultrasonic technology.

5.1.5 Coating

Line pipe is externally coated to inhibit corrosion by preventing moisture from coming into direct contact with the steel.
Normally, this is done at the mill where the pipe is manufactured or at another coating facility location before it is delivered to the construction site.
All coated pipe, however, has uncoated areas three to six inches from each end to prevent the coating from interfering with the welding process. Once the welds are made, a coating crew coats the field joint, the area around the weld, before the pipeline is lowered into the ditch.


Fig (5-4) Coating Process

Pipeline companies use several different types of coatings for field joints, the most common being fusion bond epoxy or polyethylene heat-shrink sleeves. Prior to application, the coating crew thoroughly cleans the bare pipe with a power wire brush or sandblast to remove any dirt, mill scale or debris. The crew then applies the coating and allows it to dry prior to lowering the pipe in the ditch. Before the pipe is lowered into the trench, the coating of the entire pipeline is inspected to ensure it is free of any defects.
5.1.6 Lowering In

Lowering the welded pipe into the trench demands close coordination and skilled operators. Using a series of side-booms, which are tracked construction equipment with a boom on the side, operators simultaneously lift the pipe and carefully lower the welded sections into the trench. Non-metallic slings protect the pipe and coating as it is lifted and moved into position.
In rocky areas the contractor may place sandbags or foam blocks at the bottom of the trench prior to lowering-in to protect the pipe and coating from damage.



Fig (5-5) Lowering In Process

5.1.7 Backfilling

Once the pipe has been placed in the trench, the trench can be backfilled. This is accomplished with either a backhoe or padding machine depending on the soil makeup. As with previous construction crews, the backfilling crew takes care to protect the pipe and coating as the soil is returned to the trench. As the operations begin, the soil is returned to the trench in reverse order, with the subsoil put back first, followed by the topsoil.
This ensures the topsoil is returned to its original position. In areas where the ground is rocky and coarse, crews screen the backfill material to remove rocks, or bring in clean fill to cover the pipe or the pipe is covered with a material to protect it from sharp rocks. Once the pipe is sufficiently covered, the coarser soil and rock can be used to complete the backfill.

Fig (5-6) Backfilling Process

5.1.8 Hydrostatic Test

Before the pipeline is put into natural gas service, the entire length of the pipeline is pressure tested using water. The hydrostatic test is the final construction quality assurance test. Requirements for this test are also prescribed in DOT’s federal regulations. Depending on the varying elevation of the terrain along the pipeline and the location of available water sources, the pipeline may be divided into sections to facilitate the test.
Each section is filled with water and pressured up to a level higher than the maximum operating pressure. The test pressure is held for a specific period of time to determine if it meets the design strength requirements and if any leaks are present. Once a test section successfully passes the hydrostatic test, water is emptied from the pipeline in accordance with state and federal requirements. The pipeline is then dried to assure it has no water in it before gas is put into the pipeline.

5.1.9 Restoration

The final step in the construction process is restoring the land as closely as possible to its original condition. Depending on the project’s requirements, this process typically involves decompacting the construction work areas, replacing topsoil, removing large rocks that may have been brought to the surface, completing any final repairs to irrigation systems or drain tiles, applying lime or fertilizer, restoring fences, etc.

The restoration crew carefully grades the right-of-way and in hilly areas, installs erosion-prevention measures such as interceptor dikes, which are small earthen mounds constructed across the right-of-way to divert water



Fig (5-7) restoration Process

The restoration crew also installs riprap, consisting of stones or timbers, along streams and wetlands to stabilize soils.
As a final measure the crew may plant seed and mulches the construction right-of-way to restore it to its original condition

• SPECIAL CONSTRUCTION TECHNIQUES

5.1.10 Open Cut River and Stream Crossings

This crossing method involves excavating a trench across the bottom of the river or stream to be crossed with the pipeline. Depending on the depth of the water, the construction equipment may have to be placed on barges or other floating platforms to excavate the pipe trench. If the water is shallow enough, the contractor can divert the water flow with dams and flume pipe to allow backhoes, working from the banks or the streambed, to dig the trench.
The contractor prepares the pipe for the crossing by stringing it out on one side of the stream or river and then welding, coating and hydrostatically testing the entire pipe segment. Sidebooms carry the pipe segment into the stream bed, similar to construction on land, or the construction crew floats the pipe into the river with flotation devices and positions it for burial in the trench. Concrete weights or concrete coating ensure the pipe will stay in position at the bottom of the trench once the contractor removes the flotation devices.

5.1.11 Directional Drilling

Another crossing method is the use of directional drilling. While not always feasible, this method avoids the excavation of a trench across the bottom of the crossing. It is a method considered for longer crossings and requires special geological conditions at the crossing location. Basically, it involves drilling a hole large enough for the pipeline to be pulled through it and in the shape established by the designers.

Fig (5-8) Directional Drilling Process

5.1.12 Wetlands

"Pipelining" in wetlands or marshes requires another special construction technique. In one technique, crews place large timber mats ahead of the construction equipment to provide a stable working platform. The timber mats act much like snowshoes, spreading the weight of the construction equipment over a broad area. The mats make it possible to operate the heavy equipment on the unstable soils.

5.1.13 Road Bores


For crossing most small roads pipeline contractors use the "open-cut" method. Traffic is diverted while the contractor digs the trench across the road and installs the pipeline. The contractor subsequently repairs the road bed and replaces the pavement.
For highways and major roads with heavy traffic, pipeline contractors often use road bores to install the pipeline. Similar to a directional drill for river crossings, the road bore is accomplished with a horizontal drill rig, or boring machine. The boring machine drills a hole under the road to allow insertion of the pipe. In some instances a casing is first installed in the hole, and the gas pipeline is inserted inside the casing. The benefit of the road bore is that it allows installation of the pipeline without disrupting traffic.

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Corrosion Prevention

By retarding either the anodic or cathodic reactions the rate of corrosion can be reduced. This can be achieved in several ways :
4.3.1 Conditioning the Metal
This can be sub-divided into two main groups:
(a) Coating the metal, in order to interpose a corrosion resistant coating between metal and environment. The coating may consist of:
(i) another metal , e.g. zinc or tin coatings on steel,
(ii) a protective coating derived from the metal itself,
e.g. aluminium oxide on “anodised” aluminium,
(iii) organic coatings, such as resins, plastics, paints, enamel, oils and greases.
The action of protective coatings is often more complex than simply providing a barrier between metal and environment. Paints may contain a corrosion inhibitor
ALSO……
Underbody structural components are typically coated to provide a first line of defense against corrosion. For light truck frames, the two most common coatings are hot melt wax and electrocoat (E-coat). Paints are also used on current light truck frames. Conversion coatings enhance the adhesion of electrocoat or paint, and they are commonly used in conjunction with these two coating types. Many underbody structural components, such as front rails on passenger cars, are made from sheet steel pre-coated with a metallic coating, e.g., galvanized or galvanneal sheet steel. Autophoretic and powder coatings are also used on underbody structural components.

*Coating type : 1. Internal Lining





Fig (4-1) internal coat

Description:
Internal coating using a two component liquid epoxy based paint.
Features:
This coating system has excellent anti-friction properties and good resistance to chemicals.


2. Fusion Bonded Epoxy (FBE) Powder Coating


Fig (4-2) Fusion Bonded Epoxy (FBE) Powder Coating
Description:
Stand alone coating system.
Features:
This coating system has adequate mechanical properties and effective anti-corrosion properties with resistance to high temperature operating service up to 120°C depending on raw materials used.

3. Dual Fusion Bonded Epoxy (D-FBE ) coating


Fig (4-3) Dual Fusion Bonded Epoxy (D-FBE ) coating

Description:
2-layer coating system composed of FBE primer (first layer), FBE topcoat (top layer).
Features:
This coating system has good mechanical properties and effective anti-corrosion properties and resistance to high temperature operating service up to 110°C or 150°C depending on raw materials used.

4. Bitumen / Asphalt Enameln (AE) Coating

Fig (4-4) Bitumen / Asphalt Enameln (AE) Coating

Description:
Multi-layer coating system composed of synthetic primer (first layer), enamel / inner wrap / enamel layer(s) (second and, if any following layers) and outer wrap layer (top layer).
Features:
This coating system has adequate mechanical properties and effective anti-corrosion properties with resistance to temperature operating service up to 90°C.



5. Three Layer Polypropylene (3LPP) Coating



Fig (4-5) Three Layer Polypropylene (3LPP) Coating

Description:
3-layer coating system composed of FBE primer (first layer), polypropylene based adhesive copolymer (second layer) and polypropylene based topcoat (top layer).
Features:
This coating system combines excellent mechanical properties and resistance to high temperature operating service up to 110°C or 150°C depending on raw materials used.


6. Three Layer Polyethylene (3LPE) Coating



Fig (4-6) Three Layer Polyethylene (3LPE) Coating

Description:
3-layer coating system composed of FBE primer (first layer), polyethylene based adhesive copolymer (second layer) and polyethylene based topcoat (top layer).
Features:
This coating system combines excellent mechanical properties and resistance to temperature operating service up to 60°C (LDPE & MDPE) or 80°C (HDPE) depending on raw materials used.

7. Concrete Weight Coating (CWC)



Fig (4-7) Concrete Weight Coating (CWC)

Description:
Weight coating system composed of cement, water, aggregates, heavy or light depending on the required density, and reinforcement.
Features:
Concrete weight coating is used to provide pipe stability on the sea bed as well as superior mechanical protection. It can be manufactured in a range of densities to suit the project specification.
8. Polyurethane Insulation Coating



Fig (4-8) Polyurethane Insulation Coating

Description:
2-layer coating system composed of FBE and syntactic polyurethane. Polymer or glass microspheres are blended to provide excellent thermal insulation properties.
Features:
Polyurethane insulation systems are designed to cover various water depths. Shallow water products (SPU) are based on a PU matrix into which polymer microspheres are blended to provide excellent thermal insulation properties. Deepwater applications (DWPU) are addressed using a range of products into which glass microspheres are blended. Both products have extensive track records.

9. Polypropylene Insulation Coating


Fig (4-9) Polypropylene Insulation Coating

Description:
Multi-layer coating system composed of polypropylene outer shield, solid polypropylene and foamed polypropylene / syntactic polypropylene.
Features:
Solid polypropylene is used as both anti-corrosion coating and thermal insulation coating where the thermal requirements are not too demanding. Another coating system is side extruded polypropylene foam which is used for thermal insulation of pipelines for water depths up to 600m. Syntactic polypropylene is used to achieve a balance between good thermal performance and thermal insulation capability for deepwater applications.

(b) Alloying the metal
to produce a more corrosion resistant alloy, e.g. stainless steel, in which ordinary steel is alloyed with chromium and nickel. Stainless steel is protected by an invisibly thin, naturally formed film of chromium oxide Cr2O3


4.3.2 Conditioning the Corrosive Environment


(a) Removal of Oxygen
By the removal of oxygen from water systems in the pH range 6.5 - 8.5 one of the components required for corrosion would be absent. The removal of oxygen could be achieved by the use of strong reducing agents e.g. sulphite. However, for open evaporative cooling systems this approach to corrosion prevention is not practical since fresh oxygen from the atmosphere will have continual access.
(b) Corrosion Inhibitors
A corrosion inhibitor is a chemical additive, which, when added to a corrosive aqueous environment, reduces the rate of metal wastage. It can function in one of the following ways:
(i) anodic inhibitors :
as the name implies an anodic inhibitor interferes with the anodic process.
Fe Fe++ + 2e- eq (4-1)
If an anodic inhibitor is not present at a concentration level sufficient to block off all the anodic sites, localised attack such as pitting corrosion can become a serious problem due to the oxidising nature of the inhibitor which raises the metal potential and encourages the anodic reaction (equation 1). Anodic inhibitors are thus classified as “dangerous inhibitors”. Other examples of anodic inhibitors include orthophosphate, nitrite, ferricyanide and silicates.
(ii) cathodic inhibitors :
the major cathodic reaction in cooling systems is the reduction of oxygen.
½ O2 + H2O + 2e 2OH- eq (4-2)
There are other cathodic reactions and additives that suppress these reactions called cathodic inhibitors. They function by reducing the available area for the cathodic reaction. This is often achieved by precipitating an insoluble species onto the cathodic sites. Zinc ions are used as cathodic inhibitors because of the precipitation of Zn(OH)2 at cathodic sites as a consequence of the localised high pH. (See reaction eq(4-2) ). Cathodic inhibitors are classed as safe because they do not cause localised corrosion.
(iii) adsorption type corrosion inhibitors:
many organic inhibitors work by an adsorption mechanism. The resultant film of chemisorbed inhibitor is then responsible for protection either by physically blocking the surface from the corrosion environment or by retarding the electrochemical processes. The main functional groups capable of forming chemisorbed bonds with metal surfaces are amino (NH2), carboxyl (COOH), and phosphonate (PO3H2) although other functional groups or atoms can form co-ordinate bonds with metal surfaces.
(iv) mixed inhibitors :
because of the danger of pitting when using anodic inhibitors alone, it became common practice to incorporate a cathodic inhibitor into formulated performance was obtained by a combination of inhibitors than from the sum of the individual performances. This observation is generally referred to a ‘synergism’ and demonstrates the synergistic action which exists between zinc and chromate ions.
ALSO….. CORROSION INHIBITORS
It is well known in surface chemistry that surface reactions are strongly affected by the presence of foreign molecules. Corrosion processes, being surface reactions, can be controlled by compounds known as inhibitors which adsorb on the reacting metal surface.
The term adsorption refers to molecules attached directly to the surface, normally only one molecular layer thick, and not penetrating into the bulk of the metal itself. The technique of adding inhibitors to the environment of a metal is a well known method of controlling corrosion in many branches of technology. A corrosion inhibitor may act in a number of ways: it may restrict the rate of the anodic process or the cathodic process by simply blocking active sites on the metal surface. Alternatively it may act by increasing the potential of the metal surface so that the metal enters the passivation region where a natural oxide film forms. A further mode of action of some inhibitors is that the inhibiting compound contributes to the formation of a thin layer on the surface which stifles the corrosion process.
4.3.3 Electrochemical Control
Since corrosion is an electrochemical process its progress may be studied by measuring the changes which occur in metal potential with time or with applied electrical currents. Conversely, the rate of corrosion reactions may be controlled by passing anodic or cathodic currents into the metal. If, for example, electrons are passed into the metal and reach the metal/electrolyte interface (a cathodic current) the anodic reaction will be stifled while the cathodic reaction rate increases. This process is called cathodic protection and can only be applied if there is a suitable conducting medium such as earth or water through which a current can flow to the metal to be protected In most soils or natural waters corrosion of steel is prevented if the potential of the metal surface is lowered by 300 or 400 mV. Cathodic protection may be achieved by using a DC power supply (impressed current) or by obtaining electrons from the anodic dissolution of a metal low in the galvanic series such as aluminium, zinc or magnesium (sacrificial anodes). Similar protection is obtained when steel is coated with a layer of zinc. Even at scratches or cut edges where some bare metal is exposed the zinc is able to pass protective current through the thin layer of surface moisture.
In certain chemical environments it is sometimes possible to achieve anodic protection, passing a current which takes electrons out of the metal and raises its potential. Initially this stimulates anodic corrosion, but in favourable circumstances this will be followed by the formation of a protective oxidised passive surface film.
Also …..
Cathodic protection prevents corrosion by converting all of the anodic (active) sites on the metal surface to cathodic (passive) sites by supplying electrical current (or free electrons) from an alternate source.
Usually this takes the form of galvanic anodes which are more active than steel. This practice is also referred to as a sacrificial system, since the galvanic anodes sacrifice themselves to protect the structural steel or pipeline from corrosion. In the case of aluminum anodes, the reaction at the aluminum surface is:
4Al => 4AL+++ + 12 e- eq(4-3)
and at the steel surface,
3O2 + 12e- + 6H20 => 12OH- eq(4-4)
(Oxygen gas converted to oxygen ions which combine with water to form hydroxyl ions)
As long as the current (free electrons) is arriving at the cathode (steel) faster than oxygen is arriving, no corrosion occurs.




Fig (4-10) Sacrificial Anode CP System in Seawater

· Anodic protection
Fontana and Greene’ state that ‘anodic protection can be classed as one of the most significant advances in the entire history of corrosion science’, but point out that its adoption in corrosion engineering practice is likely to be slow. Anodic protection may be described as a method of reducing the corrosion rate of immersed metals and alloys by controlled anodic polarisation, which induces passivity. Therefore, it can be applied only to those metals and alloys that show passivity when in contact with an appropriate electrolyte. This decrease in corrosion increases the life of components/plant as well as reducing the contamination of the liquid, so is particularly beneficial in the manufacture, storage and transport of chemicals such as acids. Edeleanu first demonstrated the feasibility of anodic protection and also tested it on small-scale stainless-steel boilers used for sulphuric acid solutions .
This was probably the first industrial application, although other experimental work had been carried out elsewhere. Fortunately electrochemical tests in the laboratory can give an accurate assessment of the corrosion behaviour, and the operating parameters for a specific anodic protection system can be obtained .
· Finally the anodic protection is :
• suitable for active-passive alloys (e.g. stainless steel, nickel alloys, titanium)
• requires a broad potential range for passivity
• need sizable/expensive electrical equipment
• risky if potential “slips” into the active/pitting region
• used often for very aggressive solutions when other methods fail, e.g. for protection of tanks storing of strong acids (e.g. sulphuric, phosphoric, nitric)




READ MORE - Corrosion Prevention

 
 
 

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