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Sunday, December 7, 2008

Relief Valves

Valves [Lesson 6]

5. Relief Valves
Purpose: Relief valves are used to protect systems from over-pressure or to control processes by allowing flow to commence when a certain pressure has been reached.
Operation: Refer to Figure

A spring holds the valve disc in place against the seat. The valve, therefore, will not open until the force exerted on the valve disc by the fluid pressure exceeds the force exerted by the spring. When this occurs, flow can take place through the outlet port until the fluid pressure is reduced to below the valve operatingpressure. The spring force will then release the valve.

Relief valves operate automatically and are usually pre-set to a specified relief setting by the manufacturers or adjusted when in use, if required. Re-calibration is then required

Butterfly Valves

Valves [Lesson 4]


4. Butterfly Valves

Purpose: Butterfly valves are used for controlling flow and can act as a shutuoff ~va1ve, if the sealing arrangement is designed accordinglyThe disc or wafer rotates about a vertical axis and can be turned through 90º.

The disc seals against the opening to cut off flow and can be positioned at a point between fully closed and fully open as required.

Some butterfly valves have a direct acting lever, others are operated through gearboxes when finer control is required. In most cases, a clockwise movement will close the valve

Globe Valves

Valves [Lesson 3]

2. Globe Valves
Purpose Globe valves are used to control flow as they can operate quite safely at part openings. A good shutoff can also be achieved if required
Operation: Refer to Figure

When the hand wheel is turned clockwise, the disc is against a seat, stopping the flow. Turning the hand wheel anti-clockwise lifts the disc from its seat and allows flow to continue.

The high pressure is usually on the bottom of the plug, so that the stem, seal, etc. are not under continuous pressure.
Applications are widespread, including domestic water taps

Valves

Valves [Lesson 2]

Specific Types
1. Gate Valves

Purpose: gate valves are used when a tight shut-off is required. They must not be used for throttling (i.e. must be fully off or fully on) as a restricted flow through a gate valve will erode the seat of the wedge disc.

The wedge-shaped disc is moved up to open the valve by turning the wheel anti-clockwise. To shut off the flow, the wheel is turned fully clockwise until the disc is properly seated and covers the opening.


One common type is the rising stem type. In other designs, the wheel is fixed to the stem and rises with it.

The position of the stem/stem and hand wheel indicates whether the valve is open or shut. If the stem is raised, the valve is open.



2. Ball/Plug Valves
Purpose: Ball and plug valves are used to provide a quick, simple shut-off. They are operated by turning the ball or plug through 90º. Ball and plug valves should not be used for throttling, as a restriction in the flow will lead to erosion of the valve.
Operation: Refer to Figure

The ball or plug has an opening through the centre. When this opening is in line with the inlet and outlet ports, flow will be allowed. When the ball or plug is turned through 90; no flow can take place. Good sealing can be obtained, particularly when special sealing rings made of PTFE/Teflon are used.

Some ball and plug valves are lubricated to provide a seal and prevent wear, and should be regularly lubricated with the proper lubricant.

Valves

VALVES [Lesson 1]

Process Valve Types And Applications
Valves are used in both domestic and industrial situations to control the flow of liquids, solids and gases.

The most common and familiar valves are the taps used in the home to control the hot and cold water. In the oil industry, valves are a major element in the control of operations. In general, valves are used for one or more of three main purposes:
1. To control the rate of flow (throttle);
2. To shut off/permit flow (ON/OFF function);
3. To isolate systems and protect products.

There are a wide variety of valve types and designs available from many suppliers in a wide range of materials; the main types and their uses are
- Gate Valve: Used for shut off - ON/OFF function.
- Ball/Plug Valves: Used for shut off - ON/OFF function
- Globe Valves: Used for control of flow and shut off.
- Butterfly Valves: Used for control of flow and shut off.
- Relief Valves: Spring loaded to open at a given pressure, and used to protect systems from over-pressure.
- Check Valves: To allow flow in one direction only.
- Fusible Link Valves/Piston Operated Valves: Quick acting and used for emergency shut off.
- Twin Sea valves: Used when tight shut off required.
- Semi-Needle Valves: Used in conjunction instruments to bleed off part of the flow.
- Ball Check Valves: Used with gauge glasses as safety precaution.

There are other less commonly used types of valves.
The actual construction/design of gate valves, for example, may vary widely depending on its application,the materials used, or the manufacturer’s own special features. The basic principle, however, will be the same.

Valves can be specially made to work at high or low temperatures (cryogenic), or to very high standards for use in explosive atmospheres, or when no leakage is permissible.

Design Features

1. Internal Sealing Systems And Materials
All valves are prone to leakage as it is difficult to obtain a perfect seal, although the use of special seal materials and designs can have very good result If high security is required, use can be made of two valves in series, one to act as the main valve and the second as a back-up should the first fail.

Some valves have bleed holes installed to detect leakage across the seal. If two valves are used together, a bleed hole may be fitted in the pipe between them, which can be opened when the valves are closed to drain any leakage. (Block and Bleed valves)

2. Body/Housing Materials
A wide range of materials is used in valve manufacture, the particular material depending largely on the fluids to be handled. Iron and steel are mainly used for oil/petroleum applications with most valves being made of mild or alloy steel. Brass valves are used for water (as well as cast iron, steel and other alloys).


Stainless steel is used for acids and other corrosive liquids. Bronze is also a commonly used material which can cope with most liquids.

3. External Sealing Systems And Materials
As well as the main seal between valve and disc, wedge, etc. there are other seals required to prevent external leaks. Gaskets or ‘0’ rings are used between surfaces such as flanges, where no relative movement takes place. The main problems occur around the valve stem, which both rotates and, in some cases, moves vertically as well.

Special glands or packings are used which can be compressed by gland nuts to increase sealing. Special materials have to be used in corrosive applications, but an asbestos based fibre is a commonly used packing material with PTFE/Teflon being increasingly common. ‘O’ rings can also be used as shaft seals and are generally made of rubber.

4. Actuation of Valves
Many smaller valves are hand operated if they are accessible. Larger valves require power actuators and inaccessible valves of all types require some form of mechanical or electrical actuator. Pneumatic (compressed air) and hydraulic cylinders and mechanisms are widely used in larger applications. Smaller valves can be operated with solenoids, but larger valves require more complex motors and mechanisms for electrical power operation.

5. Standards of Manufacture
There are many standards to which valves can be made:
• Metric/Imperial dimensions;
• British Standards BS;
• German Standards DIN;
• US Standards ANSI (previously ASA)
• American Petroleum Institution API.

Care must be taken that valves, flanges, etc. and other equipment are compatible, or leakage may occur.
API flanges and other equipment are commonly used in the oil industry. The standards lay down performance requirements as well as dimensions and material. Valves are rated according to the maximum pressure and temperature at which they can safely be used.

6. Quick Closing Valves
Quick closing valves can be installed in pipelines and systems to isolate sections in case of fire, leakage or other emergencies.

A spring is usually used to operate the valve and can be released by a number of methods:
• Fire melts fusible link;
• Remote manual cable;
• Air operated actuating cylinder;
• Electrical solenoid, etc.

If the valve can be installed so that the line pressure will help to close it, this will increase the sealing capability. Swinging check valves are often used as the basis of a quick closing valve, although ball valves, plug valves and butterfly valves are also suitable.

Sizing Of Pipelines

SIZING OF PIPELINES

Oil Pipelines
Pumping a specified quantity of a given oil over a given distance may be achieved by using a large diameter pipe with a small pressure drop, or small diameter pipe with a greater pressure drop.


The first alternative will tend to a higher capital cost with lower running costs. It is necessary to strike an economic balance between these two.

There are no hard and fast rules, which can be laid down for achieving this balance. For instance, a pumping station in a populated area may consist of a simple building, involving the provision of electrically driven pumps, taking power from outside sources and little else. To obtain the same pumping power in remote or undeveloped countries would involve a considerably more complicated and expensive installation. Obviously in this latter case, it is desirable to reduce the number of pumping stations at the cost of using larger diameter piping.

Similarly, the cost of the pipeline will vary considerably, depending upon circumstances. It will be costly in highly industrialised areas, environmentally sensitive areas, offshore or in hostile, mountainous or swamp areas; cheaper in flat, soft but firm, undeveloped terrain.

Gas Pipelines
Sizing problems encountered in gas lines differ considerably from those of oil lines. A simplification results from the negligible weight of the gas as the pressure in the line is virtually independent of the ground elevation on the other hand, the compressibility of gas introduces the complication of the density decreasing and consequently the volume rate of flow increasing in the direction of flow. In an oil line of constant diameter laid on level ground, the pressure decreases uniformly with distance and the velocity stays constant whereas, in a gas line, the velocity increases as the pressure gradient decreases with an exponential, which becomes progressively steeper.

The characteristics of pumps and compressors also determine the site of any pipeline booster stations as well as the initial pipeline conditions which have to be met Pumps need to be sited in positions where they are receiving the crude oil at a pressure greater than the vapour pressure of the crude oil, whereas compressors have to be sited at a location where both the pressure and velocity of the gas are at optimum conditions.

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.

Monday, October 13, 2008

Pumps

Lesson 1 — ABOUT PUMPS

Lesson Introduction
All pumps are broadly classified into two general categories: kinetic and positive-displacement. Within these categories, there are six common classes of pumps.

In this lesson, the six classes of pumps are described and identified according to the method used to create pressure. Within each class, in turn, are several types of pumps that vary from each other by their pumping method, and consequently their operating technique. For you to work safely and efficiently in a facility, you must know about the pumps your facility uses and how they operate.

In this lesson, you will learn the categories, classes, and types of pumps. You will also learn the functions of each of the common classes of pumps.

Categories of Pumps
Pumps can be broadly classified into two categories: kinetic pumps and positive-displacement pumps.

Kinetic Pumps
A kinetic pump builds pressure by first creating high fluid velocity with a rotating element. Then the fluid velocity is converted to pressure by the shape of the discharge passage. Because the fluid1 in a kinetic pump is always free to spin unrestricted within the pump casing, the discharge may be restricted or blocked without building up excessive pressure.

Positive-displacement Pumps
A positive-displacement pump is one in which a trapped amount of liquid is forced (or displaced) from the pump as the pumping mechanism moves. In theory, pressure is limited only by the power available to move the pumping element. In practice, if the discharge of a positive displacement pump is blocked, either the pump driver will stall, or the pump will rupture to relieve the pressure

NOTE
In general practice, a relief valve is installed on the discharge of a positive-displacement pump to protect against over pressure if the discharge becomes restricted or blocked. The relief valve outlet is usually routed back into the suction line. It is a dangerous practice to intentionally block the discharge valve of a positive-displacement pump and depend on the relief valve to relieve the pressure.
1 A substance that conforms to the outline of its container and has a tendency to flow. Liquids, gases, and vapors are fluids.
2 The measure of a liquid’s force per unit area.

Six Common Classes of Pumps
There are six common classes of pumps used in the process industry:
• Centrifugal
• Axial flow
• Turbine propeller
• Reciprocating
• Rotary
• Metering

The first three classes are categorized as kinetic pumps, while the last three are positive-displacement pumps. Each of the six classes applies different methods to create pressure, and these differences significantly affect pump operation.

Tuesday, September 2, 2008

Mechanical Design, Second EditionBy Peter Childs

Mechanical Design, Second EditionBy Peter Childs
Publisher: Butterworth-Heinemann
Number Of Pages: 384
Publication Date: 2003-12-30
ISBN-10 / ASIN: 0750657715
ISBN-13 / EAN: 9780750657716
Binding: Paperback



Product Description:
This book introduces the subject of total design, and introduces the design and selection of various common mechanical engineering components and machine elements. These provide "building blocks", with which the engineer can practice his or her
art.

The approach adopted for defining design follows that developed by the SEED (Sharing Experience in Engineering Design) programme where design is viewed as "the total activity necessary to provide a product or process to meet a market need." Within this framework the book concentrates on developing detailed mechanical design skills in the areas of bearings, shafts, gears, seals, belt and chain drives, clutches and brakes, springs and fasteners. Where standard components are available from manufacturers, the steps necessary for their specification and selection are developed.

The framework used within the text has been to provide descriptive and illustrative information to introduce principles and individual components and to expose the reader to the detailed methods and calculations necessary to specify and design or select a component. To provide the reader with sufficient information to develop the necessary skills to repeat calculations and selection processes, detailed examples and worked solutions are supplied throughout the text.

This book is principally a Year/Level 1 and 2 undergraduate text. Pre-requisite skills include some year one undergraduate mathematics, fluid mechanics and heat transfer, principles of materials, statics and dynamics. However, as the subjects are introduced in a descriptive and illustrative format and as full worked solutions are provided, it is possible for readers without this formal level of education to benefit from this book. The text is specifically aimed at automotive and mechanical engineering degree programmes and would be of value for modules in design, mechanical engineering design, design and manufacture, design studies, automotive power-train and transmission and tribology, as well as modules and project work incorporating a design element requiring knowledge about any of the content described.

The aims and objectives described are achieved by a short introductory chapters on total design, mechanical engineering and machine elements followed by ten chapters on machine elements covering: bearings, shafts, gears, seals, chain and belt drives, clutches and brakes, springs, fasteners and miscellaneous mechanisms. Chapters 14 and 15 introduce casings and enclosures and sensors and actuators, key features of most forms of mechanical technology. The subject of tolerancing from a component to a process level is introduced in Chapter 16. The last chapter serves to present an integrated design using the detailed design aspects covered within the book. The design methods where appropriate are developed to national and international standards (e.g. ANSI, ASME, AGMA, BSI, DIN, ISO).

The first edition of this text introduced a variety of machine elements as building blocks with which design of mechanical devices can be undertaken. The approach adopted of introducing and explaining the aspects of technology by means of text, photographs, diagrams and step-by-step procedures has been maintained. A number of important machine elements have been included in the new edition, fasteners, springs, sensors and actuators. They are included here. Chapters on total design, the scope of mechanical engineering and machine elements have been completely revised and updated. New chapters are included on casings and enclosures and miscellaneous mechanisms and the final chapter has been rewritten to provide an integrated approach. Multiple worked examples and completed solutions are included.

* New chapters on casings and enclosures, springs, and fasteners
* New information on important machine elements such as sensors and actuators
* Clear explanation of the total mechanical design process through the use of text, photographs, diagrams, step-by-step procedures and case studies

Summary: Good General Reference
Rating: 4
This is a reasonably "up to date" reference book for general mechanical design. The book has well organized solutions that include typical trial and error calculations that are close to real life design solutions where balance between what you need and what is available is often a necessary design compromise.

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Sunday, August 31, 2008

ASHRAE Handbook 2007 - HVAC Application (SI Edition)

ASHRAE Handbook 2007

HVAC Application (SI Edition)
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2008 ASHRAE Handbook - HVAC: Systems and Equipment (SI Edition)

2008 ASHRAE Handbook - HVAC: Systems and Equipment (SI Edition)
by ASHRAE
Publisher: Amer Society of Heating
Number Of Pages:
Publication Date: 2008-06
ISBN-10 / ASIN: 1933742348
ISBN-13 / EAN: 9781933742342
Binding: Hardcover

Highlights of Revisions for 2008

The 2008 ASHRAE Handbook—HVAC Systems and Equipment discusses various systems and the equipment (components or assemblies) that comprise them, and describes features and differences. This information helps system designers and operators in selecting and using equipment. An accompanying CD-ROM contains all the volume’s chapters in both I-P and SI units.

This edition includes two new chapters, described as follows:

Chapter 16, Ultraviolet Lamp Systems, includes a review of the fundamentals of UVC germicidal energy’s impact on microorganisms; how UVC lamps generate germicidal radiant energy; common approaches to the application of UVGI systems for upper-air room, in-duct, and surface cleansing; and a review of human safety and maintenance issues.
Chapter 17, Combustion Turbine Inlet Cooling (CTIC), provides a detailed discussion of how CTIC is used to help improve combustion turbine performance.

Some of the revisions and additions to the remainder of the volume are as follows:

Chapters 1 to 5 have each been revised to include new system and process flow diagrams, plus new discussion content on commissioning, building automation, maintenance management, sustainability/green design, security, and various systems (e.g., underfloor air distribution, chilled beams).
Chapter 7, Combined Heat and Power Systems, formerly entitled Cogeneration Systems and Engine and Turbine Drives, was reorganized, as well as updated for new technology.
Chapter 11, District Heating and Cooling, has new guidance on construction cost considerations, central plants, and distribution systems.
Chapter 12, Hydronic Heating and Cooling, has revised text and figures on all aspects of system design, including design procedure, water temperatures, heat transfer, distribution losses, constant- and variable-speed pumping, sizing control valves, and terminal units.
Chapter 18, Duct Construction, has new guidance for installation of flexible ducts.
Chapter 19, Room Air Distribution Equipment, was reorganized to coordinate with its companion chapter in HVAC Applications, with added content on equipment for stratified and partially stratified systems.
Chapter 24, Mechanical Dehumidifiers and Related Components, has new content on installation and service, indoor pool dehumidifiers, and application considerations for various equipment types.
Chapter 30, Automatic Fuel-Burning Systems, extensively reorganized and revised, contains updated information on new technology and code requirements.
Chapter 31, Boilers, has new material on condensing boilers, burner types, and operating and safety controls.
Chapter 32, Furnaces, has been thoroughly revised to reflect new technology and code requirements.
Chapter 34, Chimney, Vent, and Fireplace Systems, has been reorganized for clarity and has new content on designing fireplaces and their chimneys.
Chapter 36, Solar Energy Equipment, has been reorganized and has new content on photovoltaic systems and testing/rating.
Chapter 37, Compressors, has been reorganized and has updates on bearings and variable-speed drive technology.
Chapter 38, Condensers, contains revised content on air-cooled condensers, particularly on type descriptions, heat transfer, pressure drop, testing/rating, and installation and maintenance.
Chapter 40, Evaporative Air Cooling Equipment, has a rewritten section on indirect coolers.
Chapter 42, Liquid-Chilling Systems, has new discussion on both refrigerant selection and variable-flow chilled-water systems, as well as new and improved figures.
Chapter 44, Motors, Motor Controls, and Variable-Speed Drives, has updates for new technology and codes.
Chapter 48, Unitary Air Conditioners and Heat Pumps, has new content on multisplit units, variable-refrigerant-flow (VRF) equipment, certification, and sustainability.
This volume is published, both as a bound print volume and in electronic format on a CD-ROM, in two editions: one using inch-pound (I-P) units of measurement, the other using the International System of Units (SI).


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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.

Friday, August 22, 2008

Standard Handbook for Civil Engineers

Standard Handbook for Civil Engineers
Ebook Title: Standard Handbook for Civil Engineers
Author: Jonathan T. Ricketts, M. Kent Loftin, Frederick S. Merritt
Publisher: McGraw-Hill Professional; 5 edition (December 29, 2003)
Hardcover: 1600 pages
Language: English
ISBN-10: 0071364730
ISBN-13: 978-0071364737



Ebook Description
A revision of the classic reference covering all important principles and techniques needed by practicing civil engineers. The 5th Edition incorporates changes in design and construction practices, especially in design specifications for construction materials, buildings and bridges, safety and health concerns, and the most current codes changes including ACI, AISC, ASTM, NDS for wood structures, etc. Standard Handbook for Civil Engineers, covers systems design, community and regional planning, the latest design methods for buildings, airports, highways, tunnels and bridges. It includes sections on construction equipment, construction management, materials, specifications, structural theory, geotechnical engineering, wood, concrete, steel design and construction.

This book provides code changes from the ACI, ASTM, & AISC, the most up-to-date specifications for wood construction, & recent EPA & OSHA regulations. Presents new methods for nondestructive testing of piles & applications of geosynthetics. Systems requirements: PC with 486 or higher processor, Microsoft Windows 3.1, Windows 95, or NT 3.51 or later, & 16 MB of RAM. CD-ROM. --This text refers to an out of print or unavailable edition of this title.
This new, completely updated, and expanded Fifth Edition features:
- The most recent code changes, including AIC, AISC, ASTM, NDS for Wood Structures, and more
- Current EPA and OSHA regulations
- Additional information on design build delivery systems
- Increased coverage of stormwater runoff
- Over 700 tables, formulas, and drawings to make every explanation and procedure crystal clear
- Sections on construction management; materials specifications; structural theory; wood and concrete, steel design and construction; and much more
- The latest design methods for buildings, airports, highways, tunnels, and bridges

Turn to this one-stop review of the field for simplified solutions to the hundreds of practical problems you face in your day-to-day civil engineering practice.

Ebook Review
Sci-Tech Book News : The fifth edition of this reference in civil engineering features coverage of recent code changes, including AIC, ASTM, and NDS for Wood Structures, and current EPA and OSHA regulations, plus expanded information on design build delivery systems and increased coverage of stormwater runoff. There is also new information on three-dimensional modeling of pile groups, cracking in high strength steel beams, intelligent transportation, and various types of wharf designs. Coverage encompasses fundamentals of civil engineering and the latest changes in design, construction, materials, and equipment in 23 different disciplines including systems design, geotechnical engineering, and community and regional planning. Ricketts is a consulting engineer.
Choice : ...contains much useful information and many equations, tables, and facts needed in many aspects of civil engineering...well written...easy to read...Highly recommended.
From the Back Cover : IF CIVIL ENGINEERS COULD HAVE ONLY ONE REFERENCE BOOK – THIS WOULD BE IT
About the AuthorJonathan T. Ricketts is a Consulting Engineer in Palm Beach Gardens, Florida, a registered engineer in several states, and the editor of McGraw-Hill's Building Design and Construction Handbook.
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The Handbook of Highway Engineering

The Handbook of Highway Engineering
Ebook Title: The Handbook of Highway Engineering

Author: T.F. Fwa
Publisher: CRC; 1 edition (September 28, 2005)
Hardcover: 888 pages
Language: EnglishI
SBN-10: 0849319862
ISBN-13: 978-0849319860


Ebook Description
Modern highway engineering reflects an integrated view of a road system's entire lifecycle, including any potential environmental impacts, and seeks to develop a sustainable infrastructure through careful planning and active management. This trend is not limited to developed nations, but is recognized across the globe. Edited by renowned authority T.F. Fwa, The Handbook of Highway Engineering provides a comprehensive, up-to-date treatment of all aspects of highway development and engineering. Its three sections range from consideration of socio-economic and environmental factors to design, construction, maintenance, and management. Beginning with financing, access management, environmental impacts, road safety, and noise, the book explores the expanded responsibilities of the modern highway engineer as well as the increasing trend toward privatization of project development and financing. The next section considers technical issues in highway and pavement engineering, including materials, new mechanistic-empirical design approaches, and new closed-form solutions for backcalculation as well as deflection and stress computation in multi-slab systems. Rounding out the discussion, the final section examines construction, management, performance evaluation including nondestructive testing, and a chapter devoted to highway asset management. Featuring contributions from eminent experts representing eight countries on four continents, The Handbook of Highway Engineering supplies all of the tools needed to manage the entire integrated process of modern highway development and engineering.


About The Author
T.F. Fwa is the Recipient of the ASCE 2005 Frank M. Masters Transportation Engineering Award For his innovative research on highway and airport pavements and excellence in teaching and professional activities to enhance transportation engineering. --Transportation and Development Institute of ASCE, 2005

The Electrical Engineering Handbook, 2Ed

The Electrical Engineering Handbook, Second Edition

Book Description
In 1993, the first edition of The Electrical Engineering Handbook set a new standard for breadth and depth of coverage in an engineering reference work. Now, this classic has been substantially revised and updated to include the latest information on all the important topics in electrical engineering today. Every electrical engineer should have an opportunity to expand his expertise with this definitive guide.In a single volume, this handbook provides a complete reference to answer the questions encountered by practicing engineers in industry, government, or academia. This well-organized book is divided into 12 major sections that encompass the entire field of electrical engineering, including circuits, signal processing, electronics, electromagnetics, electrical effects and devices, and energy, and the emerging trends in the fields of communications, digital devices, computer engineering, systems, and biomedical engineering. A compendium of physical, chemical, material, and mathematical data completes this comprehensive resource. Every major topic is thoroughly covered and every important concept is defined, described, and illustrated. Conceptually challenging but carefully explained articles are equally valuable to the practicing engineer, researchers, and students.A distinguished advisory board and contributors including many of the leading authors, professors, and researchers in the field today assist noted author and professor Richard Dorf in offering complete coverage of this rapidly expanding field. No other single volume available today offers this combination of broad coverage and depth of exploration of the topics. The Electrical Engineering Handbook will be an invaluable resource for electrical engineers for years to come.
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