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(1)

FUNDAMENTALS OF

CONTROL VALVES

(2)

CONTROL VALVE

A CONTROL VALVE IS A FINAL

CONTROL ELEMENT AND A POWER

OPERATED DEVICE WHICH

MODIFIES THE FLOW RATE

IN A PROCESS CONTROL SYSTEM.

(3)

ROLE OF A CONTROL VALVE

It is used for

The correct distribution and control of

Flowing fluid or gases

Reduction of Pressure

As a variable orifice

(4)

CONTROL VALVE PARTS

1. BODY

2. VALVE

(5)

The body is the pressure carrying part and it

meets all their applicable pressure,

temperature and corrosion requirements.

THE BODY PROVIDES

THE PIPING CONNECTING ENDS

FLUID FLOW PASSAGE WAY, AND

SUPPORT THE SEATING SURFACE

THE VALVE CLOSURE MEMBER

(6)

INLET OUTLET STEM WITH PLUG

GLAND

PACKING BODY FLANGE

SEAT

(7)

TRIM

The trim of the valve consists of all the

parts which will be wetted other than the

body and the bonnet

Trim is the heart of the valve with a

primary function to proportion the valve

orifice in such a manner that a

prescribed relationship exists between

flow capacity and valve plug lift

(8)

The trim includes Seat, Plug, Stem,

Gland Follower, Gland Nut, Plug, Guide

Bushings and Cage

Stuffing box components considered as

trim are the packing, follower, Spring,

Lantern Ring, and Packing Retaining

Ring.

Secondary trim parts are stem to plug

attachments , seat retaining ring, seat

to body seals and spacers.

(9)

.

YOKE

A STRUCTURE BY WHICH THE

DIAPHRAGM ASSEMBLY IS SUPPORTED

RIGIDLY ON THE BONNET ASSEMBLY

(10)

TRAVEL SCALE SPRING

ADJUSTMENT SPRING BASE NUT

STEM COUPLING POINTER

ACTUATOR BASE

BONNET BASE

(11)
(12)

.

ACTUATOR

UTILISES AIR PRESSURE / ELECTRIC POWER HYDRAULIC PRESSURE

TO ACT ON A DIAPHRAGM / PISTON AND DEVELOP A FORCE TO MOVE THE

(13)

• ■ PNUEMATICALLY OPERATED DIAPHARGM ACTUATOR

PNUEMATICALLY OPERATED CYLINDER ACTUATOR

MOTOR OPERATED PISTON ACTUATOR HYDRAULIC OPERATED PISTON

ACTUATOR

ACTUTATOR

(14)

DIAPHRAGM CASINGS LOCK NUT STEM CONNECTOR SPRING ADJUSTER ACTUATOR STEM ACTUATOR SPRING BONET FLANGE VENT SCALE STUFFING BOX YOKE DIAPHRAGM GLAND STUDS SPRING SEAT DIAPHRAGM PLATE INPUT SIGNAL INDICATOR

ACTUATOR PARTS

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(16)

•GLOBE •GATE •DIAPHRAGM •PINCH OR CLAMP •GLOBE •ANGLE •THREE-WAY •BALL •BUTTER FLY •PLUG •SEGMENTED BALL •FULL BALL •CYLIDRICAL •TAPERED •ECCENTRIC SPHERE •LINEAR •MOTION •ROTARY •MOTION •VALVE

(17)

B a ll B u t t e r f ly P lu g R o t a r y M o t io n G lo b e A n g le T h r e e W a y G lo b e G a te D ia p h r a g m P in c h o r C la m p L in e a r M o tio n T y p e s o f V a v le s

(18)

IT IS MOSTLY COMMONLY USED ONE.

IT IS A VALVE WITH A LINEAR CLOSURE

MEMBER

MOST COMMON TYPE CONTROL VALVE

CLASSIFIED AS

SINGLE SEATED AND

DOUBLE SEATED

SINGLE SEATED CONFORMS TIGHT SHUT OFF.

DOUBLE SEATED VALVE IS HAVING HIGH

RESISTANCE TO VIBRATION AND

ABRASION.

(19)
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(21)

IT HAVE THE ADVANTAGE OF EASY

TRIM REMOVAL .

IT IS TOP ENTRY VALVE WITH

UNBALANCED, SINGLE-SEATED TRIM.

THE INNER VALVE PARTS CAN EASILY

BE REMOVED AFTER REMOVING THE

BONNET , BECAUSE ABSENCE OF

(22)
(23)
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ANGLE VALVES ARE SUITABLE FOR SLURRY FLUID ,

ADHESIVE FLUID AND HIGH VISCOSITY LIQUIDS.

SUITABLE FOR HIGH PRESSURE APPLICATION.

(25)
(26)
(27)

IT IS SIMPLY DESIGN

EXTENSION OF DOUBLE SEATED GLOBE VALVE.

DIVIDES FLOW IN TWO

DIRECTIONS

CONVERGES TWO

STREAMS OF FLOW TO ONE

(28)

APPLICABLE WHERE STRAIGHT THROUGH FLOW

PATH , TIGHT SHUT OFF AND EASE OF OPERATION ARE REQUIRED.

MOST SUITABLE FOR HANDLING SLURRIES AS IT

MINIMISES THE TENDENCY OF THE FLUIDS TO EITHER SETTLE OR STAIN .

SUITABLE FOR HIGH FLOW CAPACITY..

(29)
(30)

     .

IT OFFERS THE ADVANTAGES OF SIMPLICITY, LOW COST, LIGHT

WEIGHT,AND SPACE SAVING.

VALVE IS SUITABLE FOR LOW PRESSURE DROP APPLICATIONS ACTUATOR TORQUE REQUIRED IS LOWEST AS COMPARED TO

OTHER VALVES .

IT HAS MAXIMUM FLOW CAPACITY .

(31)
(32)

•The most common type of rotary valve used for

control is the BUTTERFLY valve.

•The typical application range is in sizes from 2”

through 36” or larger, for low or moderate

pressures,or on unusual applications involving large

flows at high static pressures ,but with limited

(33)

IT IS THE RELATION BETWEEN THE FLOW RATE THROUGH THE CONTROL VALVE AND PLUG TRAVEL , WHEN A CONSTANT PRESSURE DIFFERENTIAL IS MAINTAINED ACROSS THE VALVE

THIS IS ACHIEVED BY VARYING THE FLUID FLOW AREA WITH RESPECT TO THE SHAPE OF THE PLUG.

THE DESIGN OF A CONTROL VALVE TRIM IS BASED ON THE FLOW CHARACTERISTICS .

DIFFERENT CHARACTERISTICS WHICH ARE COMMONLY SELECTED TWO TYPES

1. TWO POSITION (ON-OFF)CONTROL 2. THROTTLING CONTROL

(34)

•THE PLUG IS THE MOVING COMPONENT OF THE VALVE WHICH THROTTLES FLOW BY POSITIONING ITSELF WITHIN THE SEAT ORFICE AND SHUTS OFF FLOW BY CONTACTING THE SEAT. • THE PLUG IS MOVED AGAINST DYNAMIC FLUID FLOW

FORCES BY STEM FORCE TRANSMITTED FROM THE ACTUATOR. • THE PLUGS (OR CAGE SLOTS) ARE SHAPED TO THROTTLE FLOW WITH GIVEN CHARACTERSTICS SUCH AS

•QUICK OPENING, • LINEAR,

(35)

THREE TYPES OF VALVE CHARACTERESTICS ARE

•QUICK OPENING

:

This type of characteristics provides maximum change in flow rate at lower valve travels, as the plug bottom is flat with a fairly linear relationship , opening with a small signal will give the maximum flow rate

Additional increase in valve travel gives sharply reduced changes in flow rate .

(36)

•LINEAR CHARACTERSTICS:

This type of valve provides change in flow rate which is linear with the valve lift.

That is this proportional relationship produces a

characteristics with constant slope so that with constant pressure drop , the valve gain is the same at all flow

rates. Q = KX

(37)

•EQUAL PERCENTAGE :( =% )

Equal increments of valve travel produce flow changes which are equal percentage of existing flow .

The change in flow rate is always proportional to the flow rate that exits just before the change in valve position is made .

Q = Q0 emx

Q0 = minimum controllable flow rate .

(38)

Equal Percent = ( Present value - Previous value) / Previous value. Q = Flow Rate QO = Min Flow QM = Max Flow X = Valve Travel m = ln R/T m X R/T R=QM / QO T = 1 2.96 2 100 0.1 3.91 0.39 50 50 1 0.48 4.37 2 100 0.2 3.91 0.78 50 50 1 0.48 6.47 2 100 0.3 3.91 1.17 50 50 1 0.48 9.56 2 100 0.4 3.91 1.56 50 50 1 0.48 14.14 2 100 0.5 3.91 1.96 50 50 1 0.48 20.91 2 100 0.6 3.91 2.35 50 50 1 0.48 30.92 2 100 0.7 3.91 2.74 50 50 1 0.48 45.73 2 100 0.8 3.91 3.13 50 50 1 0.48 67.62 2 100 0.9 3.91 3.52 50 50 1 0.48 100.00 2 100 1.0 3.91 3.91 50 50 1

(39)

LIFT(%) LINEAR EQUAL % Q.O 10 20 30 40 50 60 70 80 10 20 30 40 50 60 70 80 2.96 4.37 6.47 9.56 14.14 20.91 30.92 45.73 07 24 45 68 83 92 95 98 •Linear •Equal %

(40)

F L O W •10 •20 •30 •40 •50 •60 •70 •80 •90 •100 •10 •20 •30 •40 •50 •60 •70 •80 •90 •100 •0

(41)

•It is the number of US gallons per minute of water at 60 degree F that will pass through flow restriction at

(42)

BASIC FLOW RATE FORMULA FOR LIQUIDS IS: Q = K* A* SQRT {(P1-P2)/G}

Q=Flow rate in gpm or Kg/hr

p1=Upstream pressure in psig or Kg/cm2 p2=Downstream pressure in psig or Kg/cm2 G=Specific gravity at referred temperature

K= DISCHARGE COEFFICIENT, A = AREA IF G =1 AND P1-P2 = 1, THEN Q = K*A

(43)

NOW Q = Cv * SQRT {(P1-P2)/G}

WHICH IS THE RELAVENT FORMULA OF FLOW COEFFICIENT OF CONTROL VALVE IN CASE OF LIQUIDS .

THE SAME PROCEDURE WILL BE ADOPTED IN CASE OF GAS FLOW , STEAM FLOW ETC. WITH SUITABLE MODIFICATION OF WORKING FORMULA.

(44)

•It is effectively an index of pressure recovery in a control valve. •i.e. High Cf values indicate low pressure recovery where a low Cf value indication of high pressure recovery .

•when fluid flows through the valve orifice , there is a marked increase in velocity . This velocity increase is accompanied by proportional decrease in pressure . Velocity reaches maximum and pressure a minimum at the smallest cross sectional flow area downstream of the orifice and that particular point is called

(45)

•ORIFICEPLATE •-- -- ---- -- ---- -- ---- -- ---- -- ---- -- ---- -- ---- -- ---- ---•PRESSURE •VELOCITY •VENA CONTRACTA •P1 •PV •P2

(46)

•Control valves give problems mainly in three areas •1. Cavitation with associate noise and vibration •2. Flashing

(47)

•Control valve selection is in step wise •step 1 : calculate CV

•1.select valve type

•step 2 : select valve size , trim size and characteristics. •Step 3 : select end connections

•1. End connection type •2. End connection rating

(48)

•Step 4 : select seat leakage •that is class1/2/3/4/5.

•Step5: select actuator type and size •step 6: select valve materials

•1. Valve body material •2.trim material

•3 seat construction as dictated by seat leakage •4. Guided bushing

(49)

•Step 7 : select packing material and bonnet type •1.packing material a)standard Teflon asbestos

•b)Teflon v- ring c)Grafoil •2. bonnet type

•standard / extended / bellows seal extension

•step8: select valve accessories •1.positioner

•2.sov / volume booster / air set / lock up valve / volume tank / limit switch / travel

(50)

•IN GENERAL, ALL MANUFACTURERS HAVE THEIR OWN DESIGN DATA SHEETS, CONSIDERING THE

CRITICAL FLOW , CAVITATION , FLASHING AND VALVE NOISE OF THE GIVEN PROCESS CONDITION •WHEN THE CALCULATED Cv VALUE IS KNOWN, SELECTION AND SIZING OF CONTROL VALVE IS EASY.

(51)

•AIR FILTER REGULATOR •VALVE POSITIONER

•VOLUME BOOSTER •QUICK EXHAUST •AIR LOCK RELAY •LIMIT SWITCHES •SOLENOID VALVE

(52)

•The main function of positioner is to ensure that the control •valve position is always proportional to the value of controller •output signal regardless of packing box friction,actuator hysteresis •the unbalanced forces of the plug.

(53)

USAGE OF VALVE POSITIONER:

• SMOOTH CONTROL

• CHANGING OF OPERATION MODE • ACHIEVING SPLIT RANGE

• REDUCING TIME LAG

• CHANGING VALVE CHARACTERSTICS

(54)

BELLO WS SPRING RESTRICTION I/P SIGNAL NOZZLE EXHAUST VALVE STROKE C.V.STEM BELLOWS DEFLECTION RELAY VALVE

(55)
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(57)

CLASS I CLASS II CLASS III CLASS IV CLASS V CLASS VI NOT SPECIFIED

0.5% RATED VALVE CAPACITY 0.1 % RATED VALVE CAPACITY 0.01% RATED VALVE CAPACITY

5*10-4ml per min. OF WATER PER

INCH OF ORIFICE DIAMETER PER PSI DIFFERENTIAL

(58)

4

2

5

4

5

2

1

3

AVOID AVOID

(59)

References

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