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    Part (2)

    VALVES

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    Chapter (1)

    Introduction

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    Introduction to Valves

    Every piping system must have some means of controlling the amount

    and direction of flow. This is accomplished with valves. Valves used in the

    machinery space piping systems, and constructed with threaded valve stems,

    must be right-hand closing (clockwise).

    Valves are usually made of bronze, brass, cast iron, malleable iron, or

    steel. Steel valves are either cast or forged, and are made of carbon steel, low

    alloy steel, or stainless steel. Alloy steel valves are used in high pressure, high

    temperature systems. The disks and seats of these valves are usually surfaced

    with a chromium-cobalt alloy known as STELLITE. This material is extremely

    hard.

    Bronze and brass valves are not used in high temperature systems or

    systems subject to high pressures, severe vibration and shock. Bronze valves

    are widely used in salt water systems. Seats and disks of bronze valves used for

    salt water service are often made ofMonel An alloy of nickel and copper and

    other metals (such as iron and/or manganese and/or aluminum) which is highly

    resistant to corrosion and erosion.

    Many different types of valves are used to control the flow of liquids and

    gases. There are two main groups of valves.

    STOP VALVES - Stop valves are used to shut off or, in some cases, partially

    shut off the flow of fluid. Stop valves are controlled by the movement of the

    valve stem.

    Stop valves can be divided into four general categories: globe, gate,

    butterfly, and ball valves. Plug valves and needle valves may also be

    considered stop valves.

    CHECK VALVES - are used to permit the flow in only one direction. These

    valves are controlled by the flow itself.

    Valve designs vary greatly due to the demands of service. Some valves

    are combinations of the basic types mentioned, and others such as pressure

    reducing valves must be considered special valves. In general however we may

    consider stop valves to include globe valves, gate valves, piston valves, plug

    valves, needle valves, and butterfly valves.

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    Check valves include swing-check and lift-check valves.

    Excessive leakage and premature failure of valve packing is an

    indication of a scored valve stem. There is another method for classification of

    valves according to the function of valves as will be explained.

    Functions of Valves

    Each valve has a particular application for which it is best suited.

    Although valves may appear the same, they are very sophisticated in some

    cases and represent a great deal of research, engineering, and testing. Five

    functions of valves listed below:

    1- Starting and Stopping Flow:

    This is the service for which valves are most generally used. Gate valves

    are excellently suited for such service. Their seating design permits fluid to

    move through the open valve in a straight line with minimum restriction of

    flow and loss of pressure at the valve. The gate principle is not practical for

    throttling.

    2- Regulating or Throttling Flow:

    Regulating throttling flow is done most efficiently with globe or angle

    valves. Their seating design causes a change in direction of flow through the

    valve body, thereby increasing resistance o flow at the vale. Globe and angle

    valve disk construction permits closer regulation of flow. These valves are

    seldom used in sizes above 12 inch due to the difficulty of opening and closing

    the larger valves against line pressure.

    3- Preventing Back Flow:

    Check valves perform the single function of checking or preventing

    reversal of flow in piping. They come in two basic types, swing check and lift

    check. Flow keeps these valves open, and gravity and reversal of flow close

    them automatically. As a general rule, swing checks are used with gate valves

    and lift checks with globe valves.

    4- Regulating pressure:

    Pressure regulators are used in lines where it is necessary to reduce

    incoming pressure to the required service pressure. They not only reduce

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    pressure but also maintain it at the point desired. Reasonable fluctuations of

    inlet pressure to a regulator valve do not affect the outlet pressure for which it

    is set.

    5- Reliving pressure:

    Boilers and other equipment subject to damage from excessive pressures

    should be equipped with safety valves or relief valves. They usually are spring-

    loaded valves, which open automatically when pressure exceeds the limit for

    which the valve is set. Safety valves are generally used for steam, air or other

    gases. Relief valves are usually used for liquids.

    Basic Types of Valves

    There are dozens of different types of valves, but nine or so are perhaps

    the most frequently used and could be considered the basic types. The basic

    types of valves shown in the next figure can be classified as the following:

    1- Globe Valve.

    2- Angle Valve.

    3- Gate Valve.

    4- Plug Valve

    5- Ball Valve.

    6- Butterfly Valve.

    7- Needle Valve.

    8- Check Valve.

    9- Relief Valve.

    Special Types of Valves

    Each manufacturer builds many valves that are considered special. By

    special, we mean that the valve does a particular job, the design is patented by

    hat manufacturer, and no one else builds one exactly like it. In order to show

    even a portion of them it would take numerous pages and explanations.

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    1- Globe Valve 2-Angle Valve. 3-Gate Valve.

    4- Plug Valve. 5-

    Ball Valve. 6 Butterfly Valve.

    7- Needle Valve. 8- Check Valve. 9- Relief Valve

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    Chapter (2)

    Different Types of

    Valves

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    1- Gate Valves

    Gate valves are one of the most common types of valves used in

    industry. With a gate valve the direction of fluid flow does not change, and thediameter through which the process fluid passes is essentially equal to that of

    the pipe. Hence, gate valves tend to have minimal pressure drop when opened

    fully.

    Gate valves are designed to minimize pressure drop across the valve in

    the fully opened position and stop the flow of fluid completely. In general, gate

    valves are not used to regulator fluid flow. A gate valve is closed when a

    tapered disk of diameter slightly larger than that of the pipe is lowered into

    position against the valve seats. The valve is fully open when the disk is pulledcompletely out of the path of the process fluid into the neck. There are two

    types of gate valves: wedge-shaped-gate type with an inclined seat, Fig. (1)

    and a double-disk parallel-seat type, Fig. (2).

    The former is the type most commonly used in industry. The wedge gate

    may be solid or split into halves by a plane perpendicular to the pipe, shown in

    figure. Disk flexibility is inherent to the split wedge design. This flexibility

    allows the split wedge to seal more easily and it reduces galling of the sealing

    surface in cases where the valve seats are angularity misaligned.

    In the double-disk parallel-seat type, the valve is closed by lowering the

    disks from the valve neck to a height equal to that of the valve seats. Once so

    positioned, an inclined-plane mounted between the two disks coverts

    downward stem force into axial force and presses the parallel disks firmly

    against the valve seats sealing the two openings. This type of valve design can

    also accommodate nonsymmetrical or angularity misaligned valve seats. Also

    there are two types of gate valve the first is rising stem and the second is non-

    rising stem, Figs. (3, 4, 5 & 6).

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    Fig. (1):Wedge-shaped-gate type with an inclined seat, Gate valve

    Fig. (2) ) Double-disk parallel-seat type,Gate Valve.

    Fig. (3) Rising Stem Gate Valve

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    Fig. (4) Non rising stem Gate valve - 4" high pressure

    Fig. (5) Rising Spindle Gate Valve Fig. (6) Fixedspindle Gate Valve

    2- Globe valves

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    Globe valves are widely used in industry to regulate fluid flow in both

    on-off and throttling service. The amount of flow restriction observed with a

    globe valve is a function of the valve disk (or globe) location relative to the

    valve seat. As can be seen in the pictures above, the valve seat and stem arerotated 90 to the pipe, see Figs. (1 & 2)). The direction of fluid flow through

    the valve changes several times, which increases the pressure drop across the

    valve. In most cases, globe valves are installed with the stem vertical and the

    higher pressure fluid stream connected to the pipe side above the disk, which

    helps to maintain a tight seal when the valve is fully closed. Traditionally the

    valve disk and seat were both metal, thought some modern designs use an

    elastomeric disk seal. These valves are inexpensive and simple to repair.

    Fig. (1) Globe valve Fig. (2) Globe valve

    Functions of Globe Valve

    A globe valve derives its name from the globular shape of its body. The

    valve body must large enough to allow the full area to open when the valve is

    in the open position. Globe valves are usually used for regulating flow;

    however, they can also be used for complete shutoff. The seating in a globe

    valve is parallel to the flow, whereas the seating in a gate valve is

    perpendicular.

    Advantages of a Globe Valve

    The principle advantage of a globe valve over a gate valve is that:

    1- Its close regulation is due to the proportional relation of the size of the

    seat opening to the number of turns of the hand wheel, which is the distinctive

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    feature of the plug type globe valve. An operator can gauge the rate of flow by

    the number of turns applied to the hand wheel.

    2- Time, work and wear are also saved because of the fewer turns required

    to operate a globe valve as compared to a gate valve. Whenever wear occurs asthe result of frequent or severe operation that the globe presents less of a

    maintenance problem than a gate valve.

    3- Seat and disk in most globe valves can be repaired without removing the

    valve from the pipeline.

    While they are not recommended where resistance to flow and pressure

    drop would be objection able, globe valves are generally ideal for throttling.

    They are also preferable where frequent operation is necessary.

    Globe Valve Installation

    A hand control valve, identified on a flow sheet with the letters H.C. is a

    globe valve with an indicator attached to it. This indicator tells the operator

    how high or low the steam is being lowered or raised.

    For layout purposes the important dimensions, such as the face-to-face

    height of stem opened and the diameter of the hand-wheel, may be found in any

    valve manufactures catalog. The majority of valve manufactures has

    standardized the face-to-face dimension, Fig. (3).

    Fig. (3) Different types of Globe Valves

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    Globe Valve Seatings

    Globe valves may be provided with either metal seatings or soft seatings. In the

    case of metal seatings, the seating stress must not only be high but also

    circumferentially uniform to achieve the desired degree of fluid tightness.These requirements have led to a number of seating designs. The ones shown in

    Figure 4 are common variations.

    Figure 4. Seating Configurations Frequently

    Employed in Globe Valves.

    Flat seatings (see Figure 4a) have the advantage over other types of seatings in

    that they align readily to each other without having to rely on close guiding ofthe disc. Also, if the disc is moved onto the seat without being rotated, the

    seatings mate without friction. The resistance of the seating material to galling

    is therefore unimportant in this case. Deformation of the roundness of the seat

    due to pipeline stresses does not interfere with the sealability of the seatings as

    long as the seat face remains flat. If flow is directed from above the seat, the

    seating faces are protected from the direct impact of solids or liquid droplets

    travelling in the fluid.

    By tapering the seatings, as shown in Figure 4b, c, and d, the seating stress fora given seating load can be greatly increased. However, the seating load can be

    translated into higher uniform seating stress only if the seatings are perfectly

    mated; that is, they must not be mated with the disc in a cocked position. Thus,

    tapered discs must be properly guided into the seat. Also, the faces of seat and

    disc must be perfectly round. Such roundness is sometimes difficult to maintain

    in larger valves where pipeline stresses may be able to distort the seat

    roundness. Furthermore, as the seatings are tightened, the disc moves further

    into the seat. Tapered seatings therefore tighten under friction even if the disc is

    lowered into the seat without being rotated. Thus the construction material forseat and disc must be resistant to galling in this case. The tapered seatings

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    shown in Figure 4b have a narrow contact face, so the seating stress is

    particularly high for a given seating load. However, the narrow seat face is not

    capable of guiding the disc squarely into the seat to achieve maximum sealing

    performance. But if the disc is properly guided, such seatings can achieve an

    extremely high degree of fluid tightness.

    On the debit side, narrow-faced seatings are more readily damaged by solids or

    liquid droplets than wide-faced seatings, so they are used mainly for gases free

    of solids and liquid droplets. To improve the robustness of tapered seatings

    without sacrificing seating stress, the seatings shown in Figure 4c are tapered

    and provided with wide faces, which more readily guide the disc into the seat.

    To achieve a high seating stress, the seat face in initial contact with the disc is

    relatively narrow, about 3 mm (18 in.) wide. The remainder of the seat-bore is

    tapered slightly steeper. As the seating load increases, the disc slips deeper intothe seat, thereby increasing the seating width. Seatings designed in this way are

    not as readily damaged by erosion as the seatings in Figure 4b. In addition, the

    long taper of the disc improves the throttling characteristic of the valve.

    Figure 5. Seatings of Globe Valves Adapted

    for Throttling Duty.

    The performance of such seatings may be improved by hollowing out the disc

    to impart some elasticity to the disc shell, as is done in the valve shown in

    Figure 6. This elasticity permits the disc to adapt more readily to deviations of

    the seatings from roundness. The seatings shown in Figure 4d are ball shaped

    at the disc and tapered at the seat. The disc can therefore roll, to some extent,

    on the seat until seat and disc are aligned. Because the contact between the

    seatings approaches that of a line, the seating stress is very high. On the debit

    side, the line contact is prone to damage from erosion. The ball-shaped seatings

    are therefore used only for dry gases, which are also free of solids. This

    construction is used mainly by U.S. manufacturers.

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    If the valve is required for fine throttling duty, the disc is frequently provided

    with a needle-shaped extension, as in the valve shown in Figure 7; or with a V-

    port skirt, as in the valve shown in Figure 8 and in the seatings shown in

    Figure 5. In the latter design, the seating faces separate before theV-ports open.

    The seating faces are, in this way, largely protected against erosion.

    An example of soft seating design is the valve shown in Figure 9. The soft

    seating insert is carried in this case by the disc, and may be renewed readily.

    Figure 6. Globe Valve, Standard Pattern, Integral Bonnet,

    Plug-Type Disc Integral with Non-Rotating Stem.

    Figure 7. Globe Valve, Angle Pattern, Screwed-in Bonnet,

    Internal Screw Needle Disc.

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    Figure 8. Globe Valve, Angle Pattern, Bolted Bonnet, External Screw, PlugDisc with V-Port Skirt for Sensitive Throttling Control.

    Figure 9. Globe Valve, Standard Pattern, Union Bonnet,

    Internal Screw and Renewable Soft Disc.

    Connection of Disc to Stem

    The stem of a globe valve may be designed to rotate while raising or lowering

    the disc, or be prevented from rotating while carrying out this task. These

    modes of stem operation have a bearing on the design of the disc-to-stem

    connection. Most globe valves incorporate a rotating stem because of simplicity

    of design. If the disc is an integral component of the stem in this case, as it

    frequently is in small needle valves such as those shown in Figure 7, the

    seatings will mate while the disc rotates, possibly resulting in severe wear of

    the seatings. Therefore, the main field of application of such valves is for

    regulating duty with infrequent shut-off duty. For all other duties involving

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    rotating stems, the disc is designed to swivel freely on the stem. However,

    swivel discs should have minimum free axial play on the stem to prevent the

    possibility of rapid reciprocating movements of the disc on the stem in the near

    closed valve position.

    Also, if the disc is guided by the stem, there should be little lateral play

    between stem and disc to prevent the disc from landing on the seat in a cocked

    position. In the case of nonrotating stems, as in the valves shown in Figures 10,

    Figure 11, Figure 12, and Figure 6, the disc may be either an integral part of

    the stem (see Figure 6) or a separate component from the stem (see Figure 10,

    Figure 11, and Figure 12). Nonrotating stems are required in valves with

    diaphragm or bellows valve stem seal, as in Figure 10 and Figure 11. They

    are also used in high pressure valves such as those shown in Figure 12 and

    Figure 6 to facilitate the incorporation of power operators.

    Figure 10. Globe Valve, Standard Pattern, Welded Bonnet, External

    Screw, Plug Disc, Bellows Stem Seal with

    Auxiliary Compression packing.

    Figure 11. Globe Valve, Oblique Pattern, Screwed-in

    and Seal-Welded Bonnet, External Screw, Plug Disc.

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    Figure 12. Globe Valve, Oblique Pattern, Pressure-Seal Bonnet, External

    Screw, with Impact Handwheel, Plug Disc.

    Stuffing Boxes and Back Seating

    Figure 13 and Figure 15 show three types of stuffing boxes, which are typical

    for valves with a rising stem. The stuffing box shown in Figure 13 is the basic

    type in which an annular chamber contains the packing between the gland at

    the top and a shoulder at the bottom. The underside of the stuffing box carries a

    back seat which, in conjunction with a corresponding seat around the stem, is

    used to isolate the packing from the system fluid when the valve is fully open.The stuffing box shown in Figure 14 is supplemented with a condensing

    chamber at the bottom. The condensing chamber served originally as a cooling

    chamber for condensable gases such as steam. In this particular case, the

    condensing chamber has a test plug, which may be removed to test the back

    seat for leak tightness.

    A third variation of the stuffing box has a lantern ring mounted between two

    packing sections, as shown in Figure 15. The lantern ring is used mainly in

    conjunction with compression packings and may serve four different purposes:

    1. As an injection chamber for a sealant or an extruded or leached-out lubricant.

    2. As a pressure chamber in which an external fluid is pressurized to a pressure

    equal to or slightly higher than the system pressure to prevent any leakage of

    the system fluid to the outside. The external fluid must thereby be compatible

    with the system fluid and harmless to the surroundings of the valve.

    3. As a sealant chamber in vacuum service into which an external fluid is fed to

    serve as a sealant.

    4. As a leakage collection chamber from which the leakage is piped to a safelocation.

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    The inclusion of the lantern ring, however, increases the depth of the packing

    column. Sidewall friction reduces the gland packing input load as the packing

    depth increases, leading to an impairment of the seal integrity.37 Replacing the

    lantern ring with a spring is used in rotating pump shaft seals

    to improve the seal integrity.

    Figure 13. Basic Stuffing Box.

    Figure 14. Stuffing Box with Condensing Chamber.

    Figure 15. Stuffing Box with Lantern Ring.

    Direction of Flow Through Globe Valves

    The question of direction of flow through globe valves has two answers. If the

    possibility exists that flow from above the disc can remove either the disc from

    the stem or a component from the disc, flow directed from below the disc is

    mandatory. In this case, hand-operated globe valves with rotating stem and

    metal seatings can be closed fluid-tight without undue effort, only if the fluid

    load on the underside of the disc does not exceed about 4060 kN (9,000

    13,000 lb).39 With a non-rotating stem and rollerbearing supported stem nut, as

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    in the valves shown in Figure 12 and Figure 6, hand operated globe valves

    with metal seatings may be closed fluid-tight against a fluid load of about 70

    100 kN (16,00022,000 lb), depending on the leakage criterion and the

    construction of the valve.

    One particular advantage of flow directed from below the disc is that the

    stuffing box of the closed valve is relieved from the upstream pressure. On the

    debit side, if the valve has been closed against a hot fluid such as steam,

    thermal contraction of the stem after the valve has been closed can be just

    enough to induce seat leakage. If flow is directed from above the disc, the

    closing force from the fluid acting on top of the disc supplements the closing

    force from the stem. Thus, this direction of flow increases greatly the sealing

    reliability of the valve. In this case, hand-operated globe valves with a rotating

    stem may be opened without excessive effort, only if the fluid load acting ontop of the disc dose not exceed about 4060 kN (9,00013,000 lb).

    If the stem is of the nonrotating type with a roller-bearing supported stem nut,

    the globe valve may be opened by hand against a fluid load of about 70100

    kN (16,00022,000 lb). If the fluid load on top of the disc is higher, a bypass

    valve may have to be provided that permits the downstream system to be

    pressurized before the globe valve is opened.

    Standards Pertaining to Globe Valves

    Appendix C provides a list of U.S. and British standards pertaining to globe

    valves.

    Applications

    Duty:

    Controlling flow

    Stopping and starting flow

    Frequent valve operation

    Service:Gases essentially free of solids

    Liquids essentially free of solids

    Vacuum

    Cryogenic

    Two-Way Globe Valve

    A two-way globe valve has one inlet port and one outlet port as shown in

    the next figure in either a straight through or angle pattern. The valve can beeither push-down-to-close or push-down-to-open. Pneumatic and electric

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    actuators with linear motion to operate globe valves are available for operation

    with many control signals, Fig. (16) .

    Fig. (16) Two-way globe valve

    3- Piston Valves

    Piston valves are closing-down valves in which a piston-shaped closure

    member intrudes into or withdraws from the seat bore, as in the valves shown

    in Figures (1, 2, 3,4 & 5). In these valves, the seat seal is achieved between the

    lateral faces of the piston and the seat bore. When the valve is being opened,flow cannot start until the piston has been completely withdrawn from the seat

    bore. Any erosive damage occurs, therefore, away from the seating surfaces.

    When the valve is being closed, the piston tends to wipe away any solids,

    which might have deposited themselves on the seat. Piston valves may thus

    handle fluids that carry solids in suspension. When some damage occurs to the

    seatings, the piston and the seat can be replaced in situ, and the valve is like

    new without any machining. Like globe valves, piston valves permit good flow

    control. If sensitive flow adjustment is required, the piston may be fitted with a

    needle shaped extension. Piston valves are also used for stopping and startingflow when flow resistance due to the tortuous flow passage is accepted.

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    Figure 1. Piston Valve, Standard Pattern, Seat Packing

    Mounted in Valve Body, Piston Pressure Unbalanced.

    Figure 2. Piston Valve, Standard Pattern, Seat Packing

    Mounted in Valve Body, Piston Pressure Balanced.

    Figure 3. Piston Valve, Adapted for Draining Vessels,

    Seat Packing Mounted in Valve Body.

    Construction

    The seatings of piston valves are formed by the lateral faces of the valve bore

    and the piston. A fluid-tight contact between these faces is achieved by a

    packing that either forms part of the valve bore, as in the valves shown in

    Figure 2 through Figure 3, or part of the piston, as in the valves shown inFigure 4 and Figure 5. Packings commonly used for this purpose are

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    compression packings based on compressed asbestos or PTFE and O-ring

    packings.

    In the case of the piston valve shown in Figure 2, the piston moves in two

    packings that are separated by a lantern ring. The lower packing represents theseat packing, while the upper packing seals the piston to the atmosphere. The

    bonnet serves thereby as the gland that permits both packings to be tightened

    through tightening of the cover bolts. Disc springs under the nuts of the cover

    bolts minimize variations in packing stress due to thermal contraction and

    expansion of the valve parts. When one of the packings leaks, the fluid seal can

    be restored by retightening the bolts. Retightening must be carried out while the

    valve is closed to prevent an unrestrained expansion of the seat packing into the

    valve bore. The valve shown in Figure 2 differs from the one in Figure 3 only

    in that the piston is pressure balanced. The two packings around the piston areboth seat packings, and a separate packing is provided for the stem.

    The purpose of balancing the piston is to minimize the operating effort in large

    valves operating against high fluid pressures. The packing train of the valve

    shown in Figure 3 is likewise stressed through the bonnet in conjunction with

    springs under the nuts of the cover bolts, or with a spring between the bonnet

    and the packing. However, as the piston moves into the final closing position, a

    shoulder on the piston contacts a compression ring on top of the packing so that

    any further progression of the piston tightens the packing still further.

    The piston valve shown in Figure 4 carries the seat packing on the end of the

    piston instead of in the valve bore. The packing is supported thereby on its

    underside by a loose compression ring. When the piston moves into the final

    closing position, the compression ring comes to rest on a shoulder in the seat

    bore so that any further progression of the piston causes the compression ring

    to tighten the packing. Because the packing establishes interference with the

    seat in the last closing stages only, the operating effort of the valve is lower

    over a portion of the piston travel than that of the foregoing valves.

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    Figure 4. Piston Valve Adapted for Draining Vessels, Seat Packing

    Mounted on Piston; the Ram-Seal Principle.

    Figure 5. Piston Valve, Standard Pattern, Seat Packing

    Mounted on Piston.

    The piston valve shown in Figure 5 also carries the seat packing on the piston.However, the loose compression ring is replaced by a friction ring that acts as a

    spring element and, as such, pre-stresses the packing. When the piston moves

    into the seat, the friction ring comes to rest in the seat bore, and any

    progression of the piston increases the packing stress. National standards that

    apply specifically to piston valves do not exist.

    Applications

    Duty:

    Controlling flow & Stopping and starting flow

    Service: Gases, Liquids, Fluids with solids in suspension & Vacuum

    4- Angle Valve

    Angle valves operate in a manner similar to that of a globe valve. Avalve stem raises and lowers a disk to control fluid flow through the valve. The

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    90 angle between the inlet and outlet pipes greatly reduces the pressure drop

    across the valve as compared to a globe valve, Fig. (1) .

    These valves have been used for flow control especially in systems

    where valve geometry or pressure drop were a concern. When flange facingsare used, this design allows for easy removal and replacement of the valve.

    Fig. (1) Angle Valves

    Function of Globe and Angle Valve

    Globe and angle valves are compact and light in weight, and they can be

    installed in less space than required for conventional valves. Their pressure-seal

    bonnet assures freedom from bonnet-joint leakage and maintenance.

    The globe and angle valve has a swivel plug type disk. These valves are

    used in high pressure service. The end-to-end dimensions are different from

    those of flanged valves.

    Function of Angle Valve

    The internal parts of an angle valve are very similar to those of a globe

    valve. The angle valve derives its name from the fact that the outlet flow leaves

    the valve 90-degree from the inlet.

    The Advantage of the Angle Valve

    1- The angle valve has considerably less turbulence, restriction of flow, and

    pressure drop than a globe valve because flow makes one less change of

    direction.

    2- Angle valves also cut down on the piping installation time, labor andmaterials.

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    3- An angle valve reduces the number of joints or potential leaks by serving

    as both a valve and a 90-degree elbow.

    4- The angle valve is available with the same seating variations as the globevalve: plug type disk, conventional disk, and composition disk.

    However, many refineries do not encourage the use of angle valves because

    of standardization programs. An angle valve can be used only at a 90-degree

    change of direction, whereas a straight-though globe valve has a more flexible

    usage, both in location and open ability, due to its more advantageous

    orientation.

    5- Needle Valve

    A needle valve is similar in principle to a globe valve except valve

    closure is achieved by lowering a slender point fitting into a conical or needle

    seat. These valves have been widely used to accurately regulate the flow of

    liquids and gases at low flow rates. The needle point of the stem and the

    conical seat are both normally metallic, though elastomeric seats have been

    used for fine adjustments, See Fig. (1).

    Fig. (1) Needle Valve

    6- Plug Valves

    Like gate valves, plug valves are essentially intended for on-off service.

    The disadvantages of using these valves for throttling device are:

    1- The internal parts wear rapidly

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    2- The flow is not a linear function of the degree of closer.

    The only primary moving part in typical plug valve is the tapered or

    cylindrical plug. This is transversely pierced to allow liquid to flow when the

    pierced section is exposed to the valve port. In simple, single-port plug valves,flow is controlled by turning the plug 90 degree.

    Plug valves can be classified as:

    1- Lubricated

    2- Non-lubricated.

    Both types are identical in operation, but differ in plug and seat design,

    see figure (1). Common lubricated plug are equipped with peripherallubrication channels is forced, under pressure, through these channels to

    provide a thin film between the plug surface and the seat wall.

    The lubricant is kept within the valve by a ball check valve in the stem.

    The lubricant reduces wear between the two surfaces and reduces friction and,

    hence, the tendency to jam. Non-lubricated plug valves must process liquid.

    Either of two methods is employed to prevent leakage and provide

    smooth operation: an elastomeric or polymeric sleeve surrounding the plug or

    an elastomeric or polymeric coating on the plug itself. Materials having self-

    lubricating properties, such as "Teflon", "Penton", " Nylon", etc., are used.

    Plug valves have the following advantages:

    1- Simple of construction.

    2- Compactness.

    Their simple seals are suitable for multi-port service. These can handle

    three to four separate streams. The most common valves are three and four-portunits handling two and three and four streams, respectively. A single four-way

    plug valve can take the place of four straight flow valves. This also reduces the

    piping and the number of fittings needed.

    Multi-port plugs, however, are more complex than single-port units.

    Although in single-port plugs, the valve can be opened or closed by a 90 turn,

    the multi-port units require intermediate positions for each stream. Suitable

    stop-tabs are normally supplied but inexperienced operators can be easily make

    mistakes.

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    Lubricated plug valves are available in sizes ranging from 1/4 to 30

    inches NPS. These normally operate at pressures up to 5500 psi (37.92 Mpa)

    and temperatures up 600 F (315 C).

    Non-lubricated plugs, particularly those using "Teflon" sleeves, arecommonly found in sizes ranging from 1/4 to 16 inches NPS. Since "Teflon"

    deforms under extreme temperature and pressure conditions, these valves are

    limits to 425 F (218 C) and 750 psi (5.17 Mpa), respectively, Fig. (2) .

    Fig. (1) Plug Valves

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    Plug Valves

    Fig. (2) Plug Valves

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    Plug or stop cock valves are one of the oldest types of valves and are still

    widely used for on-off service. Plug valves are made with both cylindrical and

    tapered plugs, see the next figure.

    Early models of the cock valve used metal-to-metal seals that were non-lubricated. This design is still used, but problems with galling and sticking limit

    their usefulness. The use of lubricant between the plug face and the seat

    eliminates most of these problems. The lubricant helps to control leakage

    around the plug, reduces wear between the valve contact surfaces, and slightly

    lifts the plug to reduce the operating torque required to operate the valve. Plug

    cock valves tend to be used for smaller flow rates, while the related ball valve

    is used for a much wider flow rate range, Fig. (3).

    Fig. (3) Plug Valves

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    7- Ball Valves

    Ball valves use a spherical element for sealing, which minimizes

    misalignment problems. These valves are limited to moderate temperature

    service (below 250 C) by the plastic seats that create a seal around the ball.

    The type of seat can vary with the valve pressure rating and materials of

    construction. Some valve seats are a single molded form, while other valve

    seats with higher pressure ratings often incorporate a trunnion design where

    each face of the ball is sealed separately. This type of design is similar to a plug

    cock valve, except the spherical sealing element in these valves is less likely to

    freeze in position. They have found applications in flow control, as well as

    on/off use in isolating a pipe stream. The pressure drop across the valve in a

    fully open position is minimal for a full-port design. However, with restricted-

    port designs the pressure drop can be significant.

    Ball Valves

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    Ball Valves.

    Ball Valves with Actuators.

    Ball Valve with Gear Operated.

    Multi port Ball Valve.

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    Ball Valve with Actuator Operated.

    Ball valves, as the name implies, are stop valves that use a ball to stop or

    start the flow of fluid. The ball, shown in the next figure, performs the same

    function as the disk in the globe valve. When the valve handle is operated to

    open the valve, the ball rotates to a point where the hole through the ball is inline with the valve body inlet and outlet. When the valve is shut, which requires

    only a 90-degree rotation of the handwheel for most valves, the ball is rotated

    so the hole is perpendicular to the flow openings of the valve body, and flow is

    stopped.

    Typical seawater ball valve.

    Most ball valves are of the quick-acting type (requiring only a

    90-degree turn to operate the valve either completely open or closed),but many are planetary gear operated. This type of gearing allows the

    use of a relatively small handwheel and operating force to operate a

    fairly large valve. The gearing does, however, increase the operating

    time for the valve.

    Some ball valves contain a swing check located within the ball

    to give the valve a check valve feature. Ball valves are normally

    found in the following systems aboard ship: seawater, sanitary, trimand drain, air, hydraulic, and oil transfer.

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    Forging brass ball valve

    Technical standard

    Nominal Pressure: 1.6Mpa Working Medium: Water, Oil, Gas

    Working Temperature: under 100C

    Parallel Pipe Thread to GB8464

    Advantage Ball Valves

    Trunnion mounted designs permit much larger sized and higher pressures

    Non-resilient and metal seats extend temperature range to 1000

    Environmental protection and emission control techniques widely

    available

    Infinite choice of materials of construction in combination with design

    options and choice of seating

    Manual, pneumatic, hydraulic and electric operators

    Top entry designs facilitate field inspection and maintenance

    Taper seating permits wide temperature cycling and reduces wear

    Erosive and viscous media easily handled

    Ball control valves deal with simple throttling and complicated process

    control systems

    Welded body ball valve

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    Bolted body ball valve - stainless steel 10"

    Bolted body ball valve - 6"

    Top entry ball valve - 24" Rising stem ball valve

    8- Butterfly Valve

    The sealing action of a butterfly valve is achieved by rotating a disk of

    approximately the same diameter as the pipe from a position in line with fluid

    flow to a position perpendicular to flow. The axial length of these valves is less

    than any other valve, which in cases where flange faces are used with large

    pipe sizes (greater than 10 inches) these valves have the lowest initial cost.

    If resilient seats or piston rings on the disk are used, these valves can be

    sealed by relatively low operating torque on the valve stem. This sealing action

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    is assisted by the fluid-pressure distribution that tends to close the valve. This

    same hydraulic unbalance requires that a latching device or worm gear be

    installed to prevent unwanted closure of manually operated valves. Though

    butterfly valves are used for low-pressure drop applications, the pressure drop

    across the valve is quite high with large flow rates as compared to a gate valve.

    Butterfly Valves

    There are three types of butterfly valves:

    1- The lug body.

    2- The wafer body.

    3- The two-flange body.

    The lug body has lugs to match the companion flanges bolting pattern, see the

    next figure (a). The wafer body does not have lugs for bolting, it simply

    sandwiches between the companion flanges, see the next figure (b). The two-

    flange body has built in flanges, see the next figure (c). Gaskets are notrequired for a butterfly valve since the valve linear itself forms a gasket on both

    flange faces. Gaskets may be used, however, for protection of the liner where

    frequent disassembly of the associated piping may be required. Thick, soft

    gaskets should be avoided. The word disk is marked on the stem below the

    flats to indicate the position of the disk.

    A butterfly valve can be used as a control valves or as a block valve if

    mounted with a diaphragm. Butterfly valves are used in water service, oil

    service, etc. They are also used a lot in commercial tanker ships. When a

    butterfly valve is in the open position, the flow runs parallel to the pipeline

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    around the disk. To shut off the flow, all that is required is a 90 degree turn,

    which places the disk against the valve liner and body.

    (a)Lug body.

    (b) Wafer body. (c) Two-flange body

    Butterfly valves have the following advantages:

    1- Compactness and simplicity.

    2- Low pressure drop.

    3- Good for slurries since they are self-cleaning.

    4- Satisfactory throttling characteristics over most of

    the range.

    Butterfly valves have the following disadvantages:

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    1- The unbalanced torque on the disk (expect when the valve is fully open or

    closed) tends to close the valve.

    2- Large valves require a large amount of force to operate the disk.

    3- Throttling characteristics are poor when the disk is less than 15 from the

    fully closed positing. A number of different methods are used to seal the disk inbutterfly valves. In light duty valves, the disk seats directly on the body wall,

    making a metal-to-metal contact. This does not normally give a bubble tight

    seal.

    For high-pressure service or where really right seals are required, the disk

    can be equipped with a resilient lip on its periphery. Alternative, seal rings can

    be incorporated into the valve wall. Butterfly valves are available in diameters

    from 1 inch to specially made units as large as 10 feet. The disk- to-wall seal is

    the limiting factor for temperature and pressure.

    Valves with metal-to-metal seals are generally able to withstand higher

    temperatures than those with resilient seating materials such as "Teflon",

    rubber or "Hypaln". Valves with seal ring insert have been used successfully at

    pressures up to 3000 psi (20.685 MPa). As explained before the butterfly valve

    are available in wafer and lug type. The Wafer valve can be installed between

    two flanges using bolts or nuts and studs. While the lug style valve have metal

    inserts installed in the valve's bolt holes and the valve is installed between two

    flanges using a separate set of bolts for each flange as seen clearly in the next

    figure.

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    Butterfly valve with Lug type.

    Butterfly valve with Wafer type.

    Butterfly Valves can be utilized Universally. Its application range includes,

    Process in the Chemical, Pharmaceutical, Power, Plant, Paper, Sugar, Drilling

    Rigs, Heating & Air Conditioning, Cooling, Water, Water Treatment Plants, &

    even in the construction industries for compress Air, Water, Fuel, Oils, Gases,

    Slurries with suitable seat (lining) & Disc material for a wide range of pressure

    & temperature. These Valves are wafer type and have been design to fit

    Without gasket between flanges.

    Specifications of some Butterfly valves : -

    TYPE Wafer type, Slim - Seal

    MOC C.I. / C.S. / SS 304 / 316

    SEATNeoprene / Nitrile / Viton / Silicon /

    PTFE

    RATING ASA 150#, 300#

    END CONNECTION Wafer type, Lags type, Flanged End

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    SIZES AVAILABLE 40MM TO 600MM

    In the next figures there is some Butterfly valves with motorized operated,

    with Gear operated and with pneumatic actuator.

    Butterfly Valve with Motorized operated.

    Butterfly Valve with Gear operated.

    Butterfly Valve with Pneumatic Actuator.