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Showing posts with label Piping. Show all posts
Showing posts with label Piping. Show all posts

Saturday, May 9, 2009

Steel Pipeline Systems [Part.2]

Coupling Procedures.
a. For 8-inch Steel Tubing. Procedures for this tubing, because of weight (210-pound tubing), are different than for lighter pipelines. A saddle-type carrying bar (Figure B-2) and one extra person in the crew are required for constructing the 8-inch tubing pipeline. This extra person is a second helper who assists in raising the new section onto the lineup cage and in lowering it. The rest of the coupling operations are the same as those for a 4- or 6-inch line. Except for size, the 8-inch lineup cage and pipe-cleaner swab are identical to those used on the smaller pipe.

Coupling procedures for 8-inch steel tubing are as follows:
■The second helper assists the wrenchman's helper to raise their end of the tubing section and guide it onto the lineup cage, while the stabber and jackman handle the other end.

■The second helper moves to the other end and assists the jackman and stabber in aligning the section, as directed by the wrenchman.
■The second helper assists the jackman and stabber in lowering the new end of the pipeline on the lazy board. Then the second helper assists the wrenchman's helper with the next section.
For 8- and 12-Inch Standard Steel Pipe and 12-Inch Steel Tubing. Do not manually handle pipe sections heavier than the 6-inch (300-pound) standard-weight pipe. Use powered equipment to off-load the pipe and couple one section at a time. You can stockpile the pipe along the pipeline trace. If you do, use a pipelayer (Figure B-3) to handle the pipe. (The pipelayer is a commercial piece of equipment that must be leased.)

Swabbing and Cleaning. The swabber and pipe-end cleaner swab all of the pipe on a load, one row at a time, in a single operation. (They can swab the pipe while it is still on the truck or in a stockpile.) With one man at each end, they insert a snake in either outside pipe of the top row and pass it through to the other end. The man at the end where the snake is coming through pulls it through the first pipe and simultaneously feeds the snake back through the next pipe in the row. The men repeat this operation until they swab all the pipes (Figure B-4).




(2) Moving the Pipe. The pipe is picked in the middle with an automatic clam-type release hook attached to the hoisting line of the stringing boom. The pipe joint is first raised only a few inches from the pipe. The swabber and pipe-end cleaner, working at opposite ends, clean and file the pipe land and groove on each end at the same time. At the same time, the wrenchman and helper (one team) and the jackman and stabber (another team) construct cribbing of 4- by 4-inch by 3-footlong blocks. This cribbing takes the place of the lazy board and pipe jack. Each of the blocks is tied together with rope. Doing so allows the wrenchman's helper to drag one cribbing set at a time when moving it to the next location.


(3) Positioning the Pipe. After the pipe ends are cleaned, the pipe section is swung into approximate alignment on the pipeline. The stabber inserts the lineup-cage snake through it (only one snake is used). The jackman and wrenchman's helper guide the pipe joint into position on the lineup cage protruding from the end of the line. The stringing-boom operator raises or lowers the load and extends or retracts the boom, as directed by the stabber or wrenchman. Once aligned, the jackman keeps the joint aligned by leaning or shoving against the end.
(4) Installing the Coupling. After tightening the coupling, the crew lifts the pipeline high enough so they can pull the cribbing stack out from under the pipeline and drag it forward (about 40 feet) to the far end of where they will install the next section. The jackman lowers the pipeline and guides it onto the cribbing stack. At the same time the stabber places the gasket inside out on the end of the pipeline. As soon as the coupling is tightened, the stabber pulls the lineup cage forward. The stabber erects the cribbing stacks while couplings are installed. As he moves forward, the wrenchman releases the pipe lifting tongs so that the pipe-stringing boom will swing back to the bolster truck for the next pipe section.

Steel Pipeline Systems [Part.1]

Steel Pipe. Steel pipe (light- and standard-gauge wall thickness) is available in 20-foot lengths with diameters of 4, 6, and 8 inches. Steel pipe is coupled using a standard, two-piece split-ring coupling. The coupling uses two half-moon sections, which are bolted together over a one-piece gasket. The average time required to couple together two sections of steel pipe is 5 minutes.

Lightweight Steel Grooved Pipe. This pipe is made of light gauge steel with API STD5L pipe nipples welded to each end. The pipe ends are single-grooved for use with bolted couplings. This pipe comes in 20-foot sections with 4-, 6-, 8-, and 12-inch nominal IDs. Because of its thin wall, lightweight steel pipe should not be buried nor used for submerged stream crossings or in populated areas and locations where fire and damage hazards are acute.

Standard-Weight Steel (API STD5L) Pipe. This regular commercial-type pipe, which is manufactured to the standards of the API, is used when lightweight pipe or tubing is unavailable or unsuitable. The pipe comes in 20-foot sections grooved for coupling and in random lengths and diameters beveled for welding.

Bolted Coupling. This is a standard, split-ring, groove-type coupling (Figure B-1). It consists of two housing segments; two bolts and nuts; and a synthetic-rubber, oil-resistant, self-sealing gasket. The coupling and gasket are designed so that the pipe joint seals under pressure and vacuum. The coupling provides a sufficient amount of angular deflection and slack adjustment for expansion and contraction of the line between adjacent joints.

When using bolted couplings, the crew consists of a crew leader, wrenchman, wrenchman's helper, stabber, jackman, swabber, and pipe-end cleaner. The bolted-coupling crew will normally require--

■Two 20-inch hinged socket wrench handles. ■Two sockets to fit size of pipeline coupling nut and wrench. ■File. ■Dauber brush. ■Lazy board. ■Two pipeline jacks with two snakes. ■Pipeline cleaner swab with one snake. ■Wooden blocks (4 by 4 by 10 inches) with carrying rope attached. ■Full half-gallon bucket or one-gallon bucket half filled with GAA grease. ■Cleaning rags.

Pipe Saw, 8-Inch Capacity for Hazardous Locations. This is a reciprocating-type saw powered by an air motor. You can cut steel, cast iron, and stainless or alloy steel pipe as well as bar stock structural and rail. Use this saw to cut out a damaged portion of pipeline when operating in hazardous locations. You can operate when clearances are at minimum and you can make a straight, right-angle cut.

Tapping Machine. This machine is used for tapping into a pressurized pipeline to establish a service tap or to install a pressure-relief device. This operation can be done without shutting down the pipeline system. The machine uses a hole saw; a holder-pilot performs the cutting operation. He retains the separated pipe after he completes the cut and allows for its removal.
The tapping machine is lightweight and easy to operate and has an adjustable automatic-feed rate for any cutting condition. The advance rate for cutting is set by the feed-adjustment knob. This knob engages a friction-type clutch that automatically regulates the feed rate. The operator loosens (slow feed) or tightens (faster feed) the feed-adjustment knob to obtain the correct amount of force for the task. The machine comes with a ratchet crank for manual operation.


Deadweight Tester. This tester is used to calibrate pressure gauges, verify the set points of spring-loaded relief valves, and provide precise pressure readings for pipelines. The tester uses known weights that directly correlate to known pressure gauges and the verification of set points for spring-loaded relief valves.


Wednesday, March 18, 2009

Steel Pipeline Systems

a. Steel Pipe. Steel pipe (light- and standard-gauge wall thickness) is available in 20-foot lengths with diameters of 4, 6, and 8 inches. Steel pipe is coupled using a standard, two-piece split-ring coupling. The coupling uses two half-moon sections, which are bolted together over a one-piece gasket. The average time required to couple together two sections of steel pipe is 5 minutes.

b.
Lightweight Steel Grooved Pipe. This pipe is made of light gauge steel with API STD5L pipe nipples welded to each end. The pipe ends are single-grooved for use with bolted couplings. This pipe comes in 20-foot sections with 4-, 6-, 8-, and 12-inch nominal IDs. Because of its thin wall, lightweight steel pipe should not be buried nor used for submerged stream crossings or in populated areas and locations where fire and damage hazards are acute.

c.
Standard-Weight Steel (API STD5L) Pipe. This regular commercial-type pipe, which is manufactured to the standards of the API, is used when lightweight pipe or tubing is unavailable or unsuitable. The pipe comes in 20-foot sections grooved for coupling and in random lengths and diameters beveled for welding.

d.
Bolted Coupling. This is a standard, split-ring, groove-type coupling (Figure B-1). It consists of two housing segments; two bolts and nuts; and a synthetic-rubber, oil-resistant, self-sealing gasket. The coupling and gasket are designed so that the pipe joint seals under pressure and vacuum. The coupling provides a sufficient amount of angular deflection and slack adjustment for expansion and contraction of the line between adjacent joints.
When using bolted couplings, the crew consists of a crew leader, wrenchman, wrenchman's helper, stabber, jackman, swabber, and pipe-end cleaner. The bolted-coupling crew will normally require--

  • Two 20-inch hinged socket wrench handles.
  • Two sockets to fit size of pipeline coupling nut and wrench.
  • File.
  • Dauber brush.
  • Lazy board.
  • Two pipeline jacks with two snakes.
  • Pipeline cleaner swab with one snake.
  • Wooden blocks (4 by 4 by 10 inches) with carrying rope attached.
  • Full half-gallon bucket or one-gallon bucket half filled with GAA grease.
  • Cleaning rags.

e. Pipe Saw, 8-Inch Capacity for Hazardous Locations. This is a reciprocating-type saw powered by an air motor. You can cut steel, cast iron, and stainless or alloy steel pipe as well as bar stock structural and rail. Use this saw to cut out a damaged portion of pipeline when operating in hazardous locations. You can operate when clearances are at minimum and you can make a straight, right-angle cut.

f.
Tapping Machine. This machine is used for tapping into a pressurized pipeline to establish a service tap or to install a pressure-relief device. This operation can be done without shutting down the pipeline system. The machine uses a hole saw; a holder-pilot performs the cutting operation. He retains the separated pipe after he completes the cut and allows for its removal.

The tapping machine is lightweight and easy to operate and has an adjustable automatic-feed rate for any cutting condition. The advance rate for cutting is set by the feed-adjustment knob. This knob engages a friction-type clutch that automatically regulates the feed rate. The operator loosens (slow feed) or tightens (faster feed) the feed-adjustment knob to obtain the correct amount of force for the task. The machine comes with a ratchet crank for manual operation.

g.
Deadweight Tester. This tester is used to calibrate pressure gauges, verify the set points of spring-loaded relief valves, and provide precise pressure readings for pipelines. The tester uses known weights that directly correlate to known pressure gauges and the verification of set points for spring-loaded relief valves.

Monday, November 10, 2008

Pipeline Pigging

Pipeline Pigging

General
Pipeline pigs and spheres are used for a variety of purposes in both liquids and natural gas pipelines.

Pigs and spheres are forced through the pipeline by the pressure of the flowing fluid. A pig usually consists of a steel body with rubber or plastic cups attached to seal against the inside of the pipeline and to allow pressure to move the pig along the pipeline. Different types of brushes and scrapers can be attached to the body of the pig for cleaning or to perform other functions.

Figure 4.28 illustrates a variety of pipeline pigs

Pipeline pigging is done for the following reasons:
• To clean up pipelines before use (foam pigs);
• To fill lines for hydrostatic testing, dewatering following hydrostatic testing, and drying and purging operations (spheres and foam pigs);
• To periodically remove wax, dirt and water from the pipeline (scraper pigs and brush pigs);• To sweep liquids from gas pipelines (spheres)
• To separate products to reduce the amount of mixing between different types of crude oil or refined products (squeegee pigs and “Go-Devil” pigs);
• To control liquids in a pipeline, including two-phase pipelines (spheres and foam pigs);
• To inspect pipelines for defects such as dents, buckles or corrosion (“intelligent-pigs or caliper pigs).

(Figure 4.29 illustrates a kaliper pig.)

Differential pressure is required to move a pig or sphere through the pipeline. The force required depends on elevation changes in the pipeline, friction between the pig and the pipe wall and the amount of lubrication available in the line. (A dry gas pipeline provides less lubrication tan a crude oil pipeline, for example).
Cups are designed to seal against the wall by making them larger than the inside diameter of the pipe. As the cups become worn, the amount of blow-by fluid by-passing the pigs increases because the seal is not as effective.

In the case of spheres, a certain amount of over-inflation is required to provide a seal. (In two-phase pipelines, spheres are sometimes under-inflated to allow some blow-by to lower the density of the fluid ahead of the sphere).

Pigs and spheres travel at about the same velocity as the fluid in the pipeline and travel speed is relatively constant.

Pigging Operations

Pigs are used in all types of pipelines to increase efficiency and avoid problems at pump or compressor stations that could result from the presence of unwanted materials. Brushes and scrapers on a cleaning pig remove dirt and scale from the pipeline walls. Brush and scraper pigs feature longitudinal boles, which pass through the body of the pig. The holes allow a flow of fluid through the pig to prevent the build-up of wax or debris in front of the pig.

A pig can remove very large amounts of debris if it is run over a long distance.

For example, assume a pig is run in a 24 in. pipeline, 100 miles long, and removes 0.016 in. of wax material from the wall of the pipeline. After 100 miles, a plug about 1,450 ft long would form. For this reason, pipelines are operated to very definite pigging programmes.Pipelines are often pigged first during testing following construction. Most pipelines are tested with water (hydrostatic testing) either in sections or over the entire length. A foam pig or pigs is normally sent ahead of the water when filling the test section to prevent mixing the test water with air in the line. Internallycoated pipelines are often flushed with water ahead of a pig to prevent debris from being dragged along the inside surface, damaging the coating.

After testing, the water is usually displaced with the fluid to be transported in the pipeline. A pig is run between the two fluids to separate them. In gas pipelines, the pig is used to “dewater” the pipeline by running it behind the test water. Additional pigs may also be run to ensure that as much moisture as possible is removed from the line.

Launching And Receiving
Equipment is required to introduce the pig into the pipeline and to retrieve the pig at the end of the segment being pigged. A launcher is required at the upstream of the section and a receiver at the down-stream end.

The distance between these pig “traps” depends on service, location of pump or compressor stations, operating procedures and the material used in the pig.

The design of pig launchers, pig traps and related equipment is done in accordance with standards developed by several organisations. Traps for brush pigs, squeegees and foam pigs include a barrel, short pup joint, a trap valve, a side valve and a bypass line. The barrel holds the pig for loading and unloading and is equipped with a quick-opening closure or blind flange. A barrel diameter larger than the diameter of the pipeline served is required in order to allow the Pig to be successfully launched or retrieved. Barrel length depends on operating procedures, service and available space.

Figure 4.30 and Figure 4.31 illustrate a pig launcher and a pig receiver respectively.

Sphere launchers are often designed for multiple sphere launching and recovery duties and the barrels for sphere launchers are typically longer than those for other types of pigs. The operator can load these magazines with several spheres that can be launched automatically. This approach is often used in two-phase pipelines where the barrels may be designed to accommodate over lo spheres. The sphere launcher consists of the barrel, a launching mechanism, an isolation valve, an equaliser valve and a reducing tee. A drain can serve as an equalizing line.
Figure 4.32 illustrates a sphere launcher/receiver system
Figure 4.34, shows a sphere being filled with antifreeze solution.


Combination pig and sphere launchers can also be designed if both cleaning pigs and spheres for liquid control are needed.

Pig Launching And Receiving Procedures
Pig launching and receiving procedures are often supervised by senior operations staff and fully monitored by all pipeline users but the actual procedures laid down for each pig launching/pig receiving facility will vary.

Pigging Problems
The pig launcher-receiver is probably the only high-pressure vessel on the facility, in hydrocarbon service, which is regularly opened to the atmosphere and then pressured as a normal operating procedure.

If the launcher/receiver is incorrectly purged and pressured, an explosion becomes a major possibility. To reduce the chances of such an incident, the relative procedures are commonly backed up by an “interlock-system”, which prevents the movement of valves and door closure devices until certain criteria have been met within the system.

Figure 4.33 illustrates the logic of a simple interlock system.

In the last decade at least two launchers have been involved in major explosions in Britain.
When pigs are launched into a pipeline there is always the possibility that the pig will stop or reduce the flow of fluid through the pipeline. The most common incidents and their causes are:

The pig fails to launch (this only becomes apparent alter the launch procedure is at its final stages. The possible causes are:
1. The pig is too small (wrong pig or under- sized) and the flow cannot pick up the pig in the launcher barrel.
2. The pig is too large, wrong pig or oversized and it is jammed in the exit to the launcher.
3. The pig is too far back in the launcher.

The pig indicator, Figure 4.35 should show that the pig has launched. They are, however, not always reliable.
The pig is launched successfully but fails to arrive on time with no major changes in pipeline pressures or flows. The possible causes are:
1. The pig is too small (wrong size) and cannot climb the riser into the receiver.
2. The pig has disintegrated into its component parts.
3. The pig is hung on a bend and the cups have “flipped” forwards to allow full flow.

The pig is launched successfully but fails to arrive on time and there is an increase in pipeline pressure drop in pipeline flow.

The possible causes are:
1. The pig has hung up on a bend or ’T ’piece (pig is too long for bend radius).
2. The wrong size of pig was launched (too large in diameter).
3. The pipeline has been dented and the pig is stuck at the damaged section.

The pigs “leap-frog” each other in the pipeline; (usually foam pigs).
The possible causes are:
1. The operator launched them 1, 3, 2 but did not realise (most common);
2. The front pig hangs up on an obstruction and is only cleared by the second pig rolling over it.
Spheres arrive with huge chunks missing. The most likely cause is that the launcher valve has taken a bite out of the sphere as it was launched.
Launcher valves are often half-cup ball valves, which rotate through 180º to launch the sphere. Oversized spheres hang over the side of the cup and are sliced as the cup rotates.

Pigs and spheres go into by-pass lines, junction ‘T pieces or other pipelines. Operator error or process upsets may often create situations where the sphere or pig can deviate from its normal path. In one known instance a 28” diameter neoprene sphere travelled into a 12” diameter pipe for some considerable distance before flow was stopped.
Whatever the “Causes” of pigging problems, the “effects” can be severe and in some instances the pipeline has had to be cut out to remove the offending pig.

Tuesday, August 26, 2008

Pipe Work

PIPE WORK

Applications
Pipework is extensively used throughout an offshore installation to move fluids and gases from one location to another. It can generally be classified into the following three broad groupings:


1. Process
Used to transport the produced fluids and gases between processing units on the platform.

2. Service
Used to convey air, water, etc. to where it is needed for processing, life support and other services or utility functions.

3. Transportation
Usually large diameter pipelines as used to carry the production products from installation to installation or from the field to the onshore terminal.

Pumps and compressors are used to drive fluids and gases along pipes and valves to route and control the various substances and ensure that they are correctly segregated from each other.
The contents of the pipework are carried at widely varying temperatures, pressures and flow rates and,therefore, different types of pipework and associated equipment are required.
Because of the inherent danger in carrying the oil and gas associated with offshore operations, the design,installation, testing and inspection of certain pipework is ngourously controlled to exacting standards, so that leakage and bursting do not occur.


Design Features

1. Pipe Materials
Pipes are made in a number of materials, the particular one chosen being dependent upon pressure,temperature, resistance to corrosion, cost etc.
The most commonly used is carbon steel and for process work, this is normally of seamless construction.
It is strong, weldable, ductile, and usually cheaper than pipe made from other materials. It can stand temperatures up to 750ºF and is used whenever it can stand the duty required of it.

Other metals and alloys are sometimes used although they tend to be more expensive. Traditionally, corer and copper alloys were used for instrument lines although they have largely been replaced by stainless steel. They are still used for heat transfer equipment because of their high thermal conductivity.
Pipe can be lined or coated with materials such as vitreous substances, to provide resistance to chemical attack, corrosion, etc.

GRP (Glass Reinforced Plastic) is commonly used offshore on smaller service/potable water lines.

2. Pipe Sizes
The wall thickness of pipe used is determined by the pipework designer, taking into account the internal pressure, mechanical stresses to which it is subjected (i.e. dead/live loads and expansion stresses), the corrosion allowance and the safety factor to be applied. Wall thickness is determined in the ANSI system by ‘Schedule Number”, Schedule 40 being the most generally used.

Pipe size is determined by the design requirements of flow rate and head loss. Pipe sizes are identified by the Nominal Pipe Size (NPS). It is common practice to refer to Nominal Pipe Sizes 0-12 inches diameter as Nominal Bore (NB) and greater than 12 inches diameter as Outside Diameter (OD).

3. Methods of Joining Pipe
There are three main methods of joining pipes together and attaching fittings to them. Lines of 2 inch or larger are usually butt-welded, this being the most economic, leak-proof method. Smaller lines are usually joined by socket-welding or screwing.

Where larger diameter piping is required to join up with flanged vessels, valves and other equipment, or where the line has to be opened for periodic cleaning, bolted flange joints are used instead of butt-welding.
These are described more fully later.

Butt-Welded Systems Fittings

Elbows: These are used for making 45º or 90º changes in the direction of the pipe run. Normally used are “long radius”, in which the centre line radius of
curvature is equal to 1 1/2 times the nominal pipe size (MPS). Also available are “short radius” in which the centre line radius of curvature is equal to the NI’S.

Reducing Elbow
This makes a change in line size together with a change in direction.

Return
A return makes a 180 change in direction and is used in the construction of heating coils, etc.

Bends
Bends are made from straight pipe and common bending radii are 3 and 5 times the NI’S (indicated by 3R and SR respectively).

Reducer
This joins a larger pipe to a smaller one.

Flange
REFER THIS ALSO
Is a welding-neck flange (the most common type) and a slip-on flange. Flanges are fitted to the ends of pipes, valves, vessels, etc. to enable them to be connected by bolting.

Tee
REFER THIS ALSOA tee is used to make a 90 branch from a main pipe run. If the branch is smaller than the main run, a reducing tee is used.

Socket-Welded and Screwed Systems
Their uses are similar to those described for butt-welded fittings.

Flanged Joints
As described earlier, flanged joints are used whenever the pipes, valves, vessels, fittings etc. require to be connected together by bolting for ease of dismantling and reassembly.
This section describes types of flanged joints, which are commonly encountered.

Flat-Face
Most commonly used for mating with non-steel flanges on the bodies of pumps, valves, etc. The gaskets used (see Gaskets below) have an outside diameter equal to that of the flange itself. This ensures an even pressure distribution across the flange and reduces the risk of cracking of cast-iron or bronze flange on tightening or from plant vibration.

Raised Face
The raised face is the most common type of flange, in which the gasket covers only the raised faces.

Ring-Type Joint (RTJ)
This is a more expensive type of joint, but it is the best type for high temperature, high pressure and corrosive use

Gaskets
Gaskets are used to make a tight leak-proof seal between two joint surfaces. For pipe flanges, the common types of gaskets are the full-face and ring types which are used for flat-face and raised-face flanges respectively.
Gaskets are made from compressed asbestos, asbestos-filled metal (spiral-wound) and other materials dependent on the conditions to which they are subjected. Spiral-wound gaskets separate cleanly and can often be re-used.
They are useful, therefore, if the joint has to be frequently disconnected. The finish on the joint faces differs according to the type of gasket to be used. A “serrated” face is used with asbestos gaskets and a “smooth” face with spiral-wound ones.

Line Isolation and Blinding
Frequently, a completely leak-proof means of stopping the flow in a line has to be made. This may be because:
• The line, or a piece of equipment in it, has to be isolated to allow maintenance work to be carried out;
• A change in the process requires that the line be closed.

Valves do not offer complete security, as there may always be some degree of leakage and therefore, the line is closed by one of the following methods:
Spectacle Plate and Line Blind: The spectacle plate can be changed over quickly without disturbing the pipework and gives immediate visual evidence of whether the line is open or blinded. it is generally preferable to the simple line blind which is only used where frequent changing is not required.

Line Blind Valve: This allows a line to be quickly and simply blinded by a process operator. There are many types, but a typical one, a spool type line blind.

Removable Spool and Blind Flanges: This method involves removing a complete section of the line between two flanges (the spool) and fitting blind flanges to close the two ends of the line. This gives a very positive visual indication that the line is closed. Blind flanges are used to close any pipe end, vessel entry, etc.

Pipe Supports
Methods of supporting pipework vary greatly, but a selection of some of the more common is covered in this section.

Support: The term “support” refers to any device used to carry the weight of the pipework. Supports are usually made from structural steel.

Hanger: A hanger is a particular type of support by which pipework is suspended from a structure.
Hangers are usually adjustable for height

Anchor: An anchor is a rigid support, which prevents transmission of movement along pipework.
Tie: An arrangement of rods, bars, etc. to restrict movement of pipework.
Dummy Leg: An extension piece of pipe or steel section welded to an elbow.
Guide or Shoe: A means of allowing a pipe to move along its length whilst restricting its lateral movements.

Operation
4.2.6.1 Checks During Operation
The operation of a piping system is dictated by the operation of the equipment, which it connects. Nevertheless, care must be taken at all times to ensure that

• The piping is not operated beyond its design range of pressure and temperature;
• All joints are checked regularly for leaks and any leaks discovered are reported immediately;
• The piping is correctly isolated and purged, if necessary, before any maintenance work is performed on it;
• Line markings are clearly visible and re-made if not;
• Any abnormal vibration, damage, missing supports, etc are reported immediately.

Maintenance and Inspection
Legislative and other statutory requirements dictate the type and frequency of maintenance and inspection required on piping systems installed on offshore Installations. This maintenance and inspection is necessary to ensure that the Certificate of Fitness of the installation in question remains valid. The responsibility for ensuring that these requirements are met does not lie with the process operator.
However, he will be involved in isolating. purging, etc. at the time the maintenance and inspection are carried out.

Liquid Pipe Flow: Pressure Drop Calculation

LIQUID PIPE FLOW: PRESSURE DROP CALCULATION

Flow Of Liquid & Compressed Gases Through Circular Pipe
A common engineering problem to be able to determine the losses (analysis), or velocity (prediction) or the conduit size (design) of a piping system. Flow in a pipe is characterized by 7 parameters: Fluid viscosity & specific gravity, Pipe internal diameter, roughness & length, Flow rate/velocity & head loss/pressure drop. Based on which of the parameters are known, four types of computational problems are identified: namely the Calculation of i) Pressure drop, ii) Flow rate, iii) the Pipe internal diameter and iv) Pipe length. This task is accomplished by appropriate rearrangement, substitution and iterative solution of the following Equations:

Reynolds Number Re=VD/ν


where
Re = Reynolds Number
Q = average flow rate
V = average flow velocity
γ = fluid specific gravity
ν = kinetic viscosity, centistokes
D = pipe inside diameter
L = pipe length
ε = absolute internal pipe roughness
ƒ = friction factor
ΔZ = change in elevation
h = pressure head
hf = head loss due to pipe friction
Lm = head losses due to fittings, valves, etc(length equivalent)
P = pressure
g = gravitation acceleration

BIBLIOGRAPHY
* Menon ES; Piping Calculations Manual; McGraw Hill, New York, 2005.
* Hicks TG; Mechanical Engineering Formulas, Pocket Guide; McGraw Hill, New York, 2003, Chapter 10.
* Menon ES; Liquid Pipeline Hydraulics; Marcel Dekker, Inc, New York, 2004.
* Hicks TG (Editor); Handbook Of Mechanical Engineering Calculations; McGraw Hill, New York, 1998, Section 8.

Liquid Pipe Flow: Pipe Length Calculation

LIQUID PIPE FLOW: PIPE LENGTH CALCULATION

Flow Of Liquid & Compressed Gases Through Circular Pipe
A common engineering problem to be able to determine the losses (analysis), or velocity (prediction) or the conduit size (design) of a piping system. Flow in a pipe is characterized by 7 parameters: Fluid viscosity & specific gravity, Pipe internal diameter, roughness & length, Flow rate/velocity & head loss/pressure drop. Based on which of the parameters are known, four types of computational problems are identified: namely the Calculation of i) Pressure drop, ii) Flow rate, iii) the Pipe internal diameter and iv) Pipe length. This task is accomplished by appropriate rearrangement, substitution and iterative solution of the following Equations:

Reynolds Number Re=VD/ν


where
Re = Reynolds Number

Q = average flow rate
V = average flow velocity
γ = fluid specific gravity
ν = kinetic viscosity, centistokes
D = pipe inside diameter
L = pipe length
ε = absolute internal pipe roughness
ƒ = friction factor
ΔZ = change in elevation
h = pressure head
hf = head loss due to pipe friction
Lm = head losses due to fittings, valves, etc(length equivalent)
P = pressure
g = gravitation acceleration


BIBLIOGRAPHY
* Menon ES; Piping Calculations Manual; McGraw Hill, New York, 2005.

* Hicks TG; Mechanical Engineering Formulas, Pocket Guide; McGraw Hill, New York, 2003, Chapter 10.
* Menon ES; Liquid Pipeline Hydraulics; Marcel Dekker, Inc, New York, 2004.
* Hicks TG (Editor); Handbook Of Mechanical Engineering Calculations; McGraw Hill, New York, 1998, Section 8.

Monday, August 25, 2008

Liquid Pipe Flow: Pipe Diameter Calculation

LIQUID PIPE FLOW: PIPE DIAMETER CALCULATION

Flow Of Liquid & Compressed Gases Through Circular Pipe
A common engineering problem to be able to determine the losses (analysis), or velocity (prediction) or the conduit size (design) of a piping system. Flow in a pipe is characterized by 7 parameters: Fluid viscosity & specific gravity, Pipe internal diameter, roughness & length, Flow rate/velocity & head loss/pressure drop. Based on which of the parameters are known, four types of computational problems are identified: namely the Calculation of i) Pressure drop, ii) Flow rate, iii) the Pipe internal diameter and iv) Pipe length. This task is accomplished by appropriate rearrangement, substitution and iterative solution of the following Equations:

Reynolds Number Re=VD/ν












where
Re = Reynolds Number
Q = average flow rate
V = average flow velocity
γ = fluid specific gravity
ν = kinetic viscosity, centistokes
D = pipe inside diameterL = pipe length
ε = absolute internal pipe roughness
ƒ = friction factorΔZ = change in elevation
h = pressure head
hf = head loss due to pipe friction
Lm = head losses due to fittings, valves, etc. (length equivalent)
P = pressure
g = gravitation acceleration

BIBLIOGRAPHY
* Menon ES; Piping Calculations Manual; McGraw Hill, New York, 2005.
* Hicks TG; Mechanical Engineering Formulas, Pocket Guide; McGraw Hill, New York, 2003, Chapter 10.
* Menon ES; Liquid Pipeline Hydraulics; Marcel Dekker, Inc, New York, 2004.
* Hicks TG (Editor); Handbook Of Mechanical Engineering Calculations; McGraw Hill, New York, 1998, Section 8.

Liquid Pipe Flow: Flow Rte Calculation

LIQUID PIPE FLOW: FLOW RATE CALCULATION

Flow Of Liquid & Compressed Gases Through Circular Pipe
A common engineering problem to be able to determine the losses (analysis), or velocity (prediction) or the conduit size (design) of a piping system. Flow in a pipe is characterized by 7 parameters: Fluid viscosity & specific gravity, Pipe internal diameter, roughness & length, Flow rate/velocity & head loss/pressure drop. Based on which of the parameters are known, four types of computational problems are identified: namely the Calculation of i) Pressure drop, ii) Flow rate, iii) the Pipe internal diameter and iv) Pipe length. This task is accomplished by appropriate rearrangement, substitution and iterative solution of the following Equations:

Reynolds Number Re=VD/ν












where
Re = Reynolds Number
Q = average flow rate
V = average flow velocity
γ = fluid specific gravity
ν = kinetic viscosity, centistokes
D = pipe inside diameter
L = pipe length
ε = absolute internal pipe roughness
ƒ = friction factor
ΔZ = change in elevation
h = pressure head
hf = head loss due to pipe friction
Lm = head losses due to fittings, valves, etc. (length equivalent)
P = pressure
g = gravitation acceleration

BIBLIOGRAPHY
* Menon ES; Piping Calculations Manual; McGraw Hill, New York, 2005.
* Hicks TG; Mechanical Engineering Formulas, Pocket Guide; McGraw Hill, New York, 2003, Chapter 10.
* Menon ES; Liquid Pipeline Hydraulics; Marcel Dekker, Inc, New York, 2004.
* Hicks TG (Editor); Handbook Of Mechanical Engineering Calculations; McGraw Hill, New York, 1998, Section 8.

Fouling

FOULING

The deposition of paraffin, salt or scale on flowline wells can materially reduce the cross-sectional area of the pipe and severely restrict flow.

Paraffin can usually be removed by scraping or by pumping hot oil or condensate through the lines. Salt and/or scale similarly may require removal by a pipeline scraper pig, or in some cases by chemical treatment. These factors should be carefully considered when designing and sizing the flowlines. If either of these factors are suspected, it may be wise to weight the estimated cleaning frequency with the cost of installing slightly larger pipelines.

Flanges

FLANGES

Introduction
Flanges are normally used to connect sections of pipe, valves, vessels or other fittings by forming a seal with either a ring or flat type gasket. They are assembled with stud bolts, which when tightened, force the two flange faces towards each other on the gasket to form a pressure tight seal. Flanges in the oil industry are classified according to their construction, pressure rating and diameter.

The two classifications of flanges are:
1. ASA (ANSI) American Nation Standards Institute.
2. API American Petroleum Institute
4.3.2 API Classification of Flanges

There are three common types of API flanges: API 2000,3000,5000 and there are two high pressure series, API 10,000 and 15,000. The number of the series indicated corresponds to the maximum working pressure expressed in psi at a temperature of l00ºF.


This maximum working pressure is affected by temperature। The maximum working pressure of the flange will be reduced by a factor of 1.8% for each 50ºF increase in temperature above 100ºF to a maximum of 450’F. The following table gives the maximum working pressure as a function of temperature.

Pressure Ratings

1. Test And Working Pressures
The hydrostatic test pressure is equal to twice the maximum working pressures for flanges of diameter below or equal to 14 inches. The test pressure is equal to 1.5 times the maximum working pressure for flanges of diameter equal to or greater than 16 inches.

2. ASA Flanges
With the exception of the ASA 150 series, the number corresponds to the maximum working pressure of the flange in psi at a temperature of 85OºF for carbon steel flanges.
To obtain the working pressure of the flange at temperature from –20 to+ 100ºF, the number is multiplied by 2.4.

For example:
ASA 300 Max WP = 2.4 x 300 = 720psi
ASA 900 Max WP = 2.24 x 900 =2160psi

The following table gives the working pressures of all flanges in this classification. The hydrostatic test pressure is equal to 1.5 times the working pressure at 100ºF.

4. Flange Physical Characteristics
To avoid any confusion when describing or ordering flanges, the following information should be given:
1. Type ASA or API;
2. Description of connection:
a) Weld neck flange
b) Slip on welding flange
c) Threaded flange
d) Blind flange.
3. Nominal diameter;
4. Number in ASA or API classification;
5. Type of face and gasket;
6. Bore if necessary;
7. Type of steel used for manufacture.

5. Flange Make-Up
To ensure that the flange will form a good seal, care should be taken when making them up. The studs should first be made hand tight with the faces of the flanges parallel to each other. The studs should then be gradually tightened in the sequence shown in the diagram below.

6. Line Pipe
Line pipe is required by the oil and gas industry to convey oil, gas, water, chemicals, etc. in its operations.

The API with cooperation of the American Gas Association has developed specifications meeting the needs of the oil and gas industry for steel and wrought-iron line pipe and published these in API standards 5L and 5LX. These provide standard dimensions, strengths and performance properties and the required thread gauging practice to ensure complete interchangeability.