Valves are the mechanisms of pipe lines or, as some might term it, the muscles of the piping system. They exist for a wide range of purposes-for flow-on, flow-off service, for reducing and controlling flow by throttling, for stabilization of flow to meet conditions of temperature, pressure and fluid level, for safety of the operator and of the public and to protect the plant. They can be operated by various methods, from hand control to remote control by an impulse supplied by a computer. They account for, on the average, somewhere in the region of 5 per cent to 6 per cent of the total installed plant or factory cost.
Valve selection is, therefore, of major importance, both from the necessity to obtain trouble-free operation of the plant and from the point of view of the overall economics involved. An incorrect choice can cause serious trouble sometimes involving major changeovers from the initial selection, and serious damage is also possible.
Arising from the requirements of industry, valve technology today is comprehensive and exacting and although basic principles and types may be comparatively few, the variations and refinements in materials of manufacture, in valve components and in methods of valve operation, are extensive. The word 'trim' is now in common use as a generic term for certain working parts of a valve, and although interpretations vary to a degree, essentially the term includes the spindle or stem, seat and disc, disc facings, etc. In particular, it is here that the user is presented with a varied selection in designs and materials of manufacture.
In some cases the choice of a type of valve will present no great difficulty, provided of course, that selection is made with some knowledge of the subject and due regard is paid to all conditions of valve operation. The majority of cases, however, do present problems of selection, very often requiring detailed guidance. This is more pertinent when valves are required in large quantities of a particular type or types as the consequences of unwise selection can then be extremely serious. The wide range can be narrowed by knowledge and experience, but in the final analysis consultation with the valve specialists is well worth while and often a necessity. It pays to bear in mind that 'the cheapest can sometimes be the dearest'.
Valve manufacture has a high level of specialisation, some firms concentrating on valves for the control of steam with all its highly specialised problems, others on water control, a number on valves for the oil industry and there are specialist manufacturers of ball, plug, and diaphragm valves and so on, the result being first-class products with high reputation.
Valves for industrial applications are in the following categories: gate valve and slide valve, plug valve and ball valve, globe, needle, and 'Y' valve, butterfly valve, diaphragm valve, and pinch valve. For prevention of backflow the check valve and foot valve, for pressure control, safety and relief valves, regulating and pressure-reducing valves, and piston valves.
Parallel slide valve (Figure 2) Here again the gate consists of one or two discs that slide between parallel body seats, but in this case there is no spreading mechanism as the conveyed fluid pressure forces the downstream face of the disc against the seat, thus providing effective closure. The valve is generally intended for control of flow of low pressure fluids, gases, and slurries where a perfectly tight closure is not absolutely essential.
Venturi type parallel slide valve (Figure 3) The inlet and outlet ends reduce to a smaller bore at the centre or throat of this valve, giving it the flow characteristics of a venturi where only a small increase in pressure drop is involved. The advantages are compactness of design and ease of operation due to the reduced throat diameter, and consequent reduction in load-area and length of valve stroke.
Sluice valve (Figure 5) This is a solid wedge gate valve principally used for waterworks purposes although also used for industrial applications. It is available in a wide range of sizes.
Lever gate valve is intended for quick operation (QO) and two principal designs exist (a) the sliding stem and (b) the rotary stem. The former is usually fitted with a vertical stem which slides instead of being turned by a screw as is done in the conventional gate valve. The stem, actuated by a hand lever, rapidly moves the gate or disc into or out of the flow passage.
Type (b) requires the rotation of a stem which is parallel to the line of flow of the valve. The disc is attached at right angles to the end of the stem or shaft and a quarter turn of the handle opens or closes the valve.
Wafer gate valve is a parallel slide valve of compact bubble-tight design, made in a wide range of sizes.
Compactness is emphasised by the face to face length of the valve which, in several designs, is less than 6 inches (150 mm) in the 8 inch (203 mm) size and only 15 inches (380 mm) in the 60 inch (1524 mm) bore size.
Jacketed gate valve for dealing with fluids which would normally solidify close to ambient temperatures.
Flush bottom outlet valve Designed for discharging fluids from the bottom of reaction and similar type vessels. The stem projects vertically downwards, the vessel contents discharging through the 'Y' outlet pipe. The valve seat is usually designed to fit flush inside the base of the vessel to avoid pocket accumulation of solid matter, and valve heads are arranged either to open upwards into the vessel or downwards into the valve body. Valves can be fitted with either rising or non-rising stems.
Another design is a seatless valve operated by movement of a vertical plunger or piston, the top of which, in the closed position, is flush with and tight to the inside bottom outlet of the vessel. The plunger enters the inside of the vessel when opened, thus clearing precipitate which may have bridged over the outlet (Figure 6).
Normal range is 1 inch (25 mm) through 8 inch (200 mm) bore. Rated pressures to 24 bar (350In/in2), Materials of manufacture: carbon steel, various grades of stainless steel, Monel, nickel and nickel alloys such as Hastelloy Brand C, Langalloy 7R, etc. The valve is also manufactured in glass in sizes up to 4 inch (100 mm) bore and with this valve the vessel it is attached to must have a glass outlet seated into the bottom outlet.
Sampling valves Small-bore valves, smaller but similar in some ways to the flush bottom outlet valve and designed to draw off 'in-line' fluid samples from a process stream.
One particular design of plastics construction is a compact three-way unit with shut-off and open positions and an additional position for recirculation, this being particularly adaptable to filter presses for determining the degree of filtration at any point in the press.
Jacketed valves Fully or partially jacketed valves used when the fluid in the pipe system has a high melting point and would tend to solidify unless precautions are taken in design. Full jackets, extending to the valve body ends, are necessary where the conditions are critical and full and uniform heating is required throughout the pipe system. Heating is by low grade steam or hot water but other heat transfer liquids such as Dowtherm and High Temperature Salt are used according to temperature requirements.
The previous text indicates that most types of valve can be obtained in jacketed form, the jackets usually being cast integral with the valve body and therefore manufactured in the same material as the valve itself.
Uses include the handling of products such as molten caustic, resins, gums, soaps, tars, waxes, molasses, etc.
Plastics valves All-plastics valves have obvious advantages for corrosive duties and where absolute cleanliness is required but they are much more limited in application than metal or plastic-lined metal valves. They are compact, lightweight, and easy to support, and are manufactured in both thermoplastics and thermosetting plastic resins, the former generally being lower in strength and more liable to heat deterioration than the thermosetting materials but they are easier and more economic in manufacture.
The thermoplastics include polyethylene, polyvinylchloride and polyvinyldichloride, styrene, acrylic, polypropylene, vinylidene chloride, etc., the thermosetting resins including polyesters, epoxies, and furanes. The most popular materials are pvc, p.p., and a.b.s. and manufacture includes major valve types, e.g., ball valves in full-bore straight-through, two-way 'L' port, three-way 'T' port, and metering patterns-these being the most widely used plastics valves in piping systems, the usual size range being 3/8 inch (10 mm) to 4 inch (100 mm) bore.
The globe valve (Figure 7), as its name implies, has a body of bulbous shape and is fitted with a disc or plug which sits into an orifice perpendicular to the axis of flow, the seat either being replaceable or machined integral with the body. The design imposes a greater pressure drop than gate, plug, or ball valves, but the shape of seat or plug can be varied to give differing flow characteristics.
A variety of compositions makes the valve adaptable to many different services and less power is required to seat tightly.
The metal disc usually has a spherical or taper seat and breaks down deposits which may form on the seat surface.
The stop-check valve incorporates a spindle which can be operated in the same manner as an ordinary globe valve and which can be adjusted for tight seating or restriction of valve lift. The spindle is not attached to the disc, but merely prevents it from rising.
Check valves are located in horizontal or vertical pipe lines according to type, and angle check valves are included in the various types. Materials of manufacture include cast iron, high grade cast iron, cast steel, forged steel, bar stock, brass, bronze, gunmetal, manganese and nickel alloys and stainless steels to resist highly corrosive fluids. Lined bodies are produced and flaps are manufactured in grades of natural and synthetic rubbers to give a wide choice of resistance against corrosive fluids.
Foot valve A type of check valve, sometimes fitted with a strainer to prevent particles passing through the valve and making its way to a suction pump or other priming mechanism. It is fitted at the bottom of a vertical suction pipe to maintain the suction head.
Piston valves A seatless valve based on a sliding piston which uncovers cylinder ports and is used extensively in hydraulic and pneumatic systems and other power equipment.
A type for wider use in services such as steam and oil and in industrial process pipe systems consists of a piston operated by the valve spindle which moves through two non-metallic resilient packing rings separated by a ported lantern bush which is an easy fit inside the body (Figure 11). The tightness of the valve is dependent upon the fit of the pistons in the valve rings.
The design is such that any scoring or erosion which may take place has no effect upon the tightness of the valve and flow resistance is at a minimum. The spindle screw is external and stuffing boxes are not required up to sizes of 2 inch (50 mm) bore. In larger sizes, balanced pistons are adopted and a stuffing box is then necessary.
Size range is 1/2 inch (12.5 mm) through 4 inch (100 mm) bore; working pressures up to 83 bar (1200lb/in2), maximum temperature 427°C, and designs include valves for high vacuum conditions.
Manufacture is in cast iron, bronze, cast steel, forged steel, and stainless steel. Designs include angle, 'Y' or oblique and quick opening patterns.
Also, hydraulic and pneumatic relief and safety valves, hydraulic check and non-return valves, and special application designs for high temperature, a dome-loaded pressure reducing valve, and pilot-operated balanced stop valves.
Working pressures are as high as 690 bar (10000lb/in2) and the valves are precision made from mild steel machined from bar or forgings, high duty bronze and stainless steel, etc.
Whatever the seat construction, globe valves are not recommended for slurries due to the ‘up and over’ design of the passage. They are widely used for controlling the flow of steam.
Globe valves are sometimes provided with wiping gear (Figure 12) designed, as the name implies, to clean the valve seat.
This is a large field and distinct from that of the manually operated valve, its growth having been rapid over the past decade and it will undoubtedly continue to expand to meet the increasing requirements of industry related to finer accuracy of control of more complicated processes, continuous plant operation and greater productivity leading to economies in product costs.
Control may be from conditions of pressure, temperature rate of flow, viscosity, specific gravity, level, pH value of the fluid, humidity, radioactivity, proportions of fluid, vapour or gas mixtures - in essence, to control potential variables to meet the process requirement either by methods of (a) 'self contained' or 'self operated' control, or by (b) the use of instruments which sense deviations from a previously set desired value and send signals through a control loop to actuate a valve. The valve then manipulates the flow to correct or set the deviation in the process variable.
As valves have already been described as the muscles of the piping system, the instruments can be termed the brains, and the control loops, the nerves.
This type of valve does not require an external power signal and they include back pressure regulating, and pressure reducing and regulating valves operated directly by the gas or fluid pressure in the pipe system; temperature regulating valves where a change in temperature conditions is converted into pressure by, for example, the expansion or contraction of a heat sensitive fluid; flow regulating valves where the flow rate is maintained constant regardless of line pressure fluctuations by, for example, maintaining a constant pressure drop across an orifice built into the regulating valve itself; maintenance and control of liquid level by float or displacement.
Safety and Relief Valves could also be included in this category, except that their purpose is protection and not process control. It is worth while looking at some of these valves in more detail.
Other designs of pressure control valves include features such as weight loading instead of spring loading as shown, pressure loaded where a constant fluid pressure is the loading element, also tight-closing, allowing no leak when valve is closed, usually single seat construction, and non-tight-closing where it is permissible to allow fluid to leak past the valve plug, usually of double seat construction.
To control temperatures in heated systems, these are constructed in much the same manner as the pressure regulating valves already described, the valve being operated by such means as a temperature change, causing the expansion or contraction of a heat-sensitive fluid which delivers an increased or decreased pressure to bellows which in turn act on the pilot valve.
These valves regulate a rate of flow of a liquid or gas and maintain this rate constant, regardless of pressure fluctuations in the piping system. Various designs exist, one type being operated by means of a constant pressure drop across an orifice, this being graduated by use of a sleeve which proportionately covers the orifice slot, setting generally being shown on a dial. Constant flow rate, despite pressure variations, is maintained by regulating the port opening of the sleeve control valve through an impeller which is spring loaded. Forces acting on the impeller are balanced so that upstream pressure acting downwards directly on the impeller is counteracted by downstream pressure across the orifice, plus the force exerted by the spring. This total force then equals the pressure drop across the orifice and a constant flow rate is maintained.
The simplest type of level controller is the ball float valve, where a floating ball attached to a lever maintains an already determined liquid level by opening or closing a piston valve.
Extensions and refinements to this principle include level measurement, direct operation of a main valve by the ball float valve, actuation of pilot valves, switches and similar devices, and the initiation of alarm signals. Variations in type include a double seating valve, pressure operated, where the float and lever actuate a pilot valve allowing line pressure to position the main valve, and a droptight valve where there is normally no leakage possible when the valve is closed.
N.B. The term 'ball valve' is still being applied to the ball float valve. This is confusing in view of the now widely used ball valves already described and used for process control in pipe lines.
The Level-Trol is a displacement type of controller, widely used because of its adaptability and flexibility for the indication or recording of liquid level as well as the functions of control of level and use as an 'on-off' unit. It is based on Archimedes' Principle of displacement of an immersed body. The principal element is the body itself, termed the displacer, which is suspended from a torsional measuring spring. The displacer always weighs more than the upward buoyant force developed by the liquid in which it is submerged and it is usually of cylindrical shape of constant cross sectional area, so that for each equal increment of submersion depth, an equal increment of buoyancy change will result, thus yielding the desired linear or proportional relationship.
The torsional spring, known as a torque tube, is designed to twist a specific amount for each increment of buoyancy change, and to be insensitive to pressure changes in the vessel. The degree of rotation of the inner end of the torque tube is in linear relationship to the degree of buoyancy. The design is such that the degree of torque tube rotation is transmitted with accuracy to the outside of the vessel and in such a way that the interior of the torque tube is carried through the vessel at atmospheric pressure.
There is a regulator for every pressure control application in the gas industry and gas regulators are available for large, high pressure transmission pipe lines, through small, medium, or low pressure distribution schemes down to consumer pressures and the range includes service and field regulators, distribution, and industrial regulators and the designs are extensively used for the control of many variables. As town gas and natural gas are used in many process industries, these regulators have industrial application.
Are used for 'on-off' service, particularly for emergency shut-off or opening and the design is principally applied to sliding stem globe valves, or similar types of valves. In this case, the valve stem is fitted with an armature which is drawn into the magnetic field of the solenoid winding when current is passed through the coil. The force exerted by a spring holds the valve plug either in the closed or open position - the solenoid therefore requires moving the valve plug against this force. Operating pressures are from extreme vacuum to as high as 690 bar (10000lb/in2) and temperatures from cryogenic service to 800°C. The usual size range is from 3/16 in to 4 in. (5 mm to 100 mm) bore. In larger valves where the operational forces are too great for a solenoid to overcome, a small pilot solenoid valve is used to control the fluid which pressurises the actuator mounted on the main valve.
Solenoid valves are available for both flameproof and non-flameproof conditions.
These satisfy the majority of applications and are the most used valves, particularly for fine and accurate control. The globe valve can be either single or double seated body dependent upon the permissible seat leakage, the magnitude of the pressure drop, the available actuator pressure, and the rangeability of control required.
If a high degree of leak tightness is necessary, then a single seated valve may require to be selected, as the leakage rate in this design can be guaranteed to be better than 0.01 per cent of the maximum capacity of the valve, whereas double seated, with the inherent difficulty of making the valve plug touch two seats at the same time, are usually only guaranteed to a leakage standard of 0.5 per cent. However, a single seated valve is hydraulically unbalanced. All the pressure drop across the valve acts on the full area of the valve seat and the force generated has to be overcome by the valve actuator - in consequence, a large and expensive actuator will be necessary. If the degree of leak tightness is not critical then a double seated design, which is semi-balanced because the inlet pressure acts in opposite directions on the two valve seats, will eliminate the majority of the unbalanced force, thereby enabling smaller actuators to be used and more accurate control to be obtained. There are alternatives to the single or double seated designs for applications where a high degree of leak tightness and high unbalanced forces are associated with each other as in the piston balanced design shown in Figure 18 and a single seated type originally designed for gaseous oxygen service but now in use in other services where the flowing medium is clean and non-corrosive.
This is of later origin than globe and 'Y' valves and is finding increasing application in the process industries because of its straight-through flow, low pressure drop, resistance to clogging, and ability to control slurries such as paper pulp and fluids with solids in suspension. Wide control rangeability is achieved by a 'V' notch making the ball of helmet shape (Figure 20). As the 'V' notch ball throttles to the closed position, it maintains a reducing-to-infinity triangular opening, which with the straight-through design of body gives the required flow characteristics for throttling control. The 'V' notch ball rotating into its seal creates a wedging and shearing effect which prevents dragging of fibrous matter or slurry between the seal and the ball, thus eliminating clogging.
The butterfly valve is a type which has always been used for control purposes. It is simple in design, with little to go wrong, can be produced for all pressures and sizes.
Although major work on main service piping only occurs when a new site is being developed or an existing site greatly expanded, good layout can have a profound effect on the flexibility of the site and the plant operations on the site. Pipes carrying HP and LP steam, condensate, fuel oil, towns water, cooling water, towns gas, compressed, air and effluent, are typical main service pipes, and on some works central distribution of inert gases or some process materials is accomplished by running special service pipes with the main services. Such pipes run from central distribution points to all areas of the site, serving existing plant and providing facilities from which new plants can be fed by tapping off or small extensions. Main electrical cables are frequently run with the service pipes to take advantage of pipe support structures or pipe trenches and provision should be made for these cables at design and construction stages. Since the pipes form part of the site materials distribution system, it is logical and usual for them to follow the road network and bring to installed or planned plants, all site services. The piping layout is thus largely settled by general site considerations rather than considerations of piping practice. Main services may be run on elevated steel pipe bridges or at ground level and it is usual to run the pipes in groups to save space. Individual pipes may be buried for protection against frost or for safety.
The pneumatic handling of bulk dry powders, flake and chip, and other materials of similar characteristics is increasing in industry. As in the conveyancing of liquids, vapours, and gases, piping and valves are extensively used, connected to equipment in a similar manner for a similar purpose.
Design, including pipe sizing, depends upon the operating pressure and the material-to-air ratio and although based on established principles of fluid dynamics the design is largely empirical and plant performance will be directly related to the quality and extent of preliminary experimental work carried out by the specialist supplier. High pressures (i.e. up to 3.4 bar) are normally preferred since they imply small pipes, compact equipment and generally, low initial overall cost.
The length of pipe involved, its route and capacity, in turn determine the required pipe diameter and air volume, and the interaction here is complex, requiring considerable work to establish theoretical relationship and the only safe method is experimental work with the particular material being considered.
Material/air ratio depends upon operating pressure - in the food industry medium density ratio of 50 is frequently used; in the chemical industry, where longer distances and greater capacity rates are involved, the material/air ratio can be up to ten times greater.
Blow lines and suction lines are designed for self-cleaning, but blow lines handling 'difficult' materials are sometimes fitted with quick release couplings at 'sweeps' or bends so that if a build up does occur then it can be easily removed. Vibrators are seldom, if ever, installed to clear lines, the principle being avoidance of blockage by careful and knowledgeable design and layout.
Jacketed pipe materials and fabrication Jacketed piping can be made in any combination of pipe sizes and commercially available materials, but certain combinations of pipe sizes have been standardised to suit the corresponding size of valve and fittings.
Larger and smaller sizes and combinations, including heavier schedules, are also manufactured.
Ideally, jacketed pipelines should be manufactured in no more than six-metre lengths.
When the process flow sheet and data are released, engineering design can be started on all activities. The most important task is to establish a rough layout for the plant and for this purpose the basic proportions of the equipment items are estimated from the flowsheet and integrated with the preliminary civil design to produce a number of possible alternative layouts. Selection of the optimum layout is made to suit the plant design and physical constraints of the site and the finally agreed rough layout is converted to a finished, firm design. All relevant requirements of civil, mechanical, instrument and electrical engineers are embodied in this final layout.
Whichever method is chosen should be governed by considering which provides the best method of communication between all designers and non-engineering staff concerned with producing the final layout or using this final layout as the basis for further work.
Figure 27 - Line Diagram Symbols for Pipework
Note that all symbols are intended to convey a rapid picture of the items to all staff; other symbols can be devised for us within any organisation.
Figure 29 - Typical Symbols used in Isometrics
Piping is an important element of every stage of project design, purchasing, and construction and is intimately linked to the other project work on equipment, electrical, instrument, and civil engineering. Work on piping is proceeding at every stage of the project partly because of the sheer volume of design and erection work noted above, but mainly because of the need to relate other project activities to the piping design. A typical Arrow Diagram and Bar Chart plan for a process plant project are shown in Figure 30(a) and (b). In these figures, many important functions on civil work, equipment, instrumentation, electrics, etc., are omitted for simplicity - only activities from these functions relating to piping are shown. Also emphasised by the Arrow Diagram is the late stage in the project when pipe erection is carried out and the difficulties of correcting design errors without delaying project completion.
Much of the work entailed in pipe work design, detailing, fabrication, and erection is, of necessity, labour intensive in that the work is basically repetitive with adherence to established designs and procedures, by which each individual pipe is detailed, part listed, fabricated, and erected as an individual item, with limited scope for radical improvement in working methods or man-hours employed. This feature of pipework generally, and the volume of pipework to be designed and erected, normally puts pipework design and erection on the critical path of the project plan.
The primary design data for any project is produced by the process design engineer who defines the processing stages for the product, specifies the type of equipment and controls needed, and provides the basic heat and mass balances on which the plant fluid flows are based. The process engineer's requirements are presented in two basic project documents - the flowsheet and the process engineering data.
The flow sheet is a simple diagrammatic picture of the plant which shows the equipment items connected by the major process pipes and containing data on the essential process control circuits or major process requirements. Simple symbols are used to represent different types of equipment items; these symbols are usually in accordance with BS 974 and a number of typical examples are shown in Figure 31. The aims of the flowsheet are to define exactly the essential requirements of the process design and to present an easily understood picture of the process stages and controls.
On small simple plants most of these data can be shown on the flowsheet without detriment, but on larger or complex plants where much process engineering data is produced, then the information shown on flow sheets is usually confined to flow rates, composition, and conditions.
Pipe fittings (not to be confused with pipe-line fittings) are prefabricated items applying to practically all types of pipes and pipe materials which, in the ultimate, make it possible to give complete flexibility of arrangement in designing any piping system. The fittings are invariably fabricated from the same material as the pipe, the same specifications, etc., applying and in fact, once the length and connection details of a straight pipe have been established on the drawing board, it then becomes a fitting - generally known as a 'straight'. Cast pipes of necessity being prefabricated, are all classed as fittings.
Standardisation has played an important role in establishing types of dimensioned fittings with consequent substantial saving of time not only on the drawing board but in all stages of pipework engineering.
Fittings are classified by method of end fixing, i.e., butt-welding, socket-welding, screwed, flanged, loose or fixed, socket and spigot, and lapped, and types by name - 90° and 45° elbows, reducing elbows, short and long bends, 180° return bends of long and short radius, branch bends, equal and unequal tees, crosses, concentric and eccentric reducers, caps, stub ends, etc.
Butt-welding fittings Figure 32 indicates the various types based on BS 1965, Part 1 for carbon steel and Part 2 for stainless steels and related to BS 806, and BS 1640 Parts 1 and 2 for steel fittings related to BS 3351. They also comply with American and Continental Standards.
These fittings form, by welding of prepared ends, a permanent pipe system and are widely used in conditions of medium and high temperature and pressure where liquids conveyed are clean and corrosion is virtually non-existent, and where it is necessary or at least highly desirable to avoid leakage at flanged joints and to minimise maintenance. The system is also less costly than its flanged counterpart.
Figure 32 - Types of Butt Welding Fittings
Pipes are sometimes referred to as tubes and the reverse also applies - in fact, it is no longer easy to distinguish and perhaps this is not of any real significance. However, a word of explanation may help to clarify matters.
Pipe is specified by stating its nominal size and it should be noted particularly that the nominal size is only approximate and is neither the inside nor the outside diameter and one requires using Standard Tables or Manufacturers' Tables to ascertain exactly these two dimensions. Pipes over 14 inches (355 mm) are generally specified on outside diameter and wall thickness.
Piping systems are interpreted as assemblies of pipe, valves, pipe fittings, flanges, bolting, gaskets, and pipe supports and the scope defines 'minimum requirements and recommended practice for the selection and application of materials and components of piping systems in petroleum refineries and petrochemical plants and the design, fabrication, installation and testing of these systems'.
Figure 33 - Types of Screwed Fittings
Figure 34 - Types of Cast-Iron Pipe Fittings
Figure 35 - Typical Range of Fittings
Fittings include a complete metric range to meet Continental standards (and future UK standards) and are also standardised for USA nominal bore pipe - also for use on copper tube. The couplings are also available in high duty bronze for use with non-ferrous pipe and aluminium for use with light alloy pipes.
Standard sizes are in mild steel, stainless steel where resistance to corrosion is required, and in brass for copper pipe.
Figure 36 - Cutting Ring Joint
Questions on Background Notes – Module 5.Unit 11
1. Briefly explain what Valves and fittings are used for.
|
2. Briefly explain a Temperature Regulating Valve.
|
|
4. Name two applications that Gas Regulators may be used.
|
5. What are Solenoid Valves used for?
|
1.
Valves and Fittings: Valves are the mechanisms of pipe lines or, as some might term it |
2.
Temperature Regulating Valve: To control temperatures in heated systems, these are constructed in
|
3.
Self Contained or Self Operated Control Valve:
|
4.
b. Domestic. |
5.
|
5. Continued.
Force exerted by a spring holds the valve plug either in the closed or |
Source: http://local.ecollege.ie/Content/APPRENTICE/liu/metalfab_notes/module5/Pipe%20Fitting_M5_U11.doc
Web site to visit: http://local.ecollege.ie/
Author of the text: indicated on the source document of the above text
If you are the author of the text above and you not agree to share your knowledge for teaching, research, scholarship (for fair use as indicated in the United States copyrigh low) please send us an e-mail and we will remove your text quickly. Fair use is a limitation and exception to the exclusive right granted by copyright law to the author of a creative work. In United States copyright law, fair use is a doctrine that permits limited use of copyrighted material without acquiring permission from the rights holders. Examples of fair use include commentary, search engines, criticism, news reporting, research, teaching, library archiving and scholarship. It provides for the legal, unlicensed citation or incorporation of copyrighted material in another author's work under a four-factor balancing test. (source: http://en.wikipedia.org/wiki/Fair_use)
The information of medicine and health contained in the site are of a general nature and purpose which is purely informative and for this reason may not replace in any case, the council of a doctor or a qualified entity legally to the profession.
The texts are the property of their respective authors and we thank them for giving us the opportunity to share for free to students, teachers and users of the Web their texts will used only for illustrative educational and scientific purposes only.
All the information in our site are given for nonprofit educational purposes