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  • 8/11/2019 Shut-Off Butterfly Valves 2 0 En

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    Notes for project planning

    Shut-off and buttery valves foropen-close applications and control mode

    Table of contents

    Introduction 2Shut-off and butterfly valves for open-close applications

    Project planning, design and dimensioning 4

    Butterfly valves for control modeProject planning, design and dimensioning 6

    I II III

    M MM

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    Notes for project planning Introduction

    Introduction

    Open-colose applications Energy savings and the reduction of the leakage losses will become ever more important inthe future. The generation outputs of boilers or chilling systems are divided up into dif ferentperformance level categories. Depending on the decline in pressure, the generators will then beswitched either on or off. The generators will be blocked in order to minimise performance loss.The leakage rate (shut-off seat) shall be kept as low as possible. The pressure loss shall alsobe low with the faucet opened completely. These are prerequisites for minimising the electricalperformance of the pumps and thus for lowering operating costs.

    Typical applications

    I II III

    M MM M

    M

    M

    M

    Boiler sequence system

    Open heat exchanger

    M

    p

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    Notes for project planning Introduction

    Detail 4

    1-part stemWafer type und Lug type:

    DN 50 to 350

    2-part stemWafer type:DN 25 to 40

    Introduction (Continued)

    Valves and actuators product range Fig. Lug typeshut-off valve with worm

    gear

    Fig. Lug typebuttery valve withSR..A-5 actuator

    Fig. Wafer typebuttery valve with

    SY.. actuator

    Installation of the shut-off and buttery valves in open systems

    The tting of a siphon is recommended for the purposeof achieving the maximum service life of the buttery

    valve (the seat should be in the water on both sides) andalso in order to be able to ensure that it is leak-proof.

    Fig. Lug type (with threads)Fig. Wafer type (with clips)Body of the shut-off and buttery valves

    Fig. Wafer typeshut-off valve with

    lever

    1 Spheroidal cast iron housing (GGG 40)2 Stainless stem, controlled in RPTFE bush

    bearing3 EPDM seat primary seal

    (leak-proof pursuant to EN 12266-1)4 EPDM seat secondary seal, seals against

    the exterior5 EPDM O-ring tertiary seal

    against exterior contamination6 Stainless valve disc7 Flange in accordance with ISO 52118 Stainless spindle safety device9 Dowel (for backlash-free rotation

    of the valve cone)

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    Project planning

    Relevant information The data, information and limit values listed on the data sheets and mounting instructions A6..and D6.. are to be taken into account and/or complied with, respectively.

    Pipeline clearances The minimum clearances between the pipelines and the walls and ceilings required for projectplanning depend not only on the valve size but also on the selected actuator.

    Design and dimensioning

    General information The valves can be used when the following values for open-close applications are complied with: The maximum flow speed of 4 m/s may not be exceeded in the valve. The valve is to be selected in such a way that the nominal pipe width corresponds to =

    nominal damper width and the pressure drop off is kept as low as possible.

    Closing pressure shut-off valves A6.. The maximum permissible closing pressure is 1200 kPa.

    Flow rate shut-off valves A6..H / A6..SA6..HL / A6..SL

    Shut-off valve Differential pressure pv100

    Type DN[mm]

    kvmax[m3/h]

    Zeta-Wert

    0,01[kPa]

    0,1[kPa]

    1[kPa]

    2[kPa]

    3[kPa]

    A625H 25 45 0.32 0.45 1.42 4.50 6.36

    Flow

    100[m3/h]

    A632H 32 55 0.55 0.55 1.74 5.50 7.78A640H 40 70 0.83 0.70 2.21 7.00 9.90 12.1A650H(L) 50 90 1.23 0.90 2.8 9.0 12.7 15.6A665H(L) 65 180 0.88 1.80 5.7 18.0 25.5A680H(L) 80 300 0.73 3.0 9.5 30 42A6100H(L) 100 580 0.47 5.8 18.3 58 82A6125H(L) 125 820 0.58 8.2 26 82A6150H(L) 150 1600 0.32 16 51 160A6125S(L) 125 820 0.58 8.2 26 82A6150S(L) 150 1600 0.32 16 51 160A6200S(L) 200 2900 0.3 29 92 290A6250S(L) 250 4400 0.32 44 139 440A6300S(L) 300 7300 0.24 73 231 730

    A6350S(L) 350 10900 0.2 109 345 1090

    Closing pressure buttery valves D6..ND6..NL

    Buttery valve Actuators

    SRF SR..A GR..A DGR..A DR.. SY1 SY2 SY3 SY4 SY5

    Type DN[mm]

    kvmax[m3/h]

    ps[kPa]

    ps[kPa]

    ps[kPa]

    ps[kPa]

    ps[kPa]

    ps[kPa]

    ps[kPa]

    ps[kPa]

    ps[kPa]

    ps[kPa]

    D625N 25 45 1200 1200 1200D632N 32 55 1200 1200 1200D640N 40 70 1200 1200 1200D650N(L) 50 90 1200 1200 1200D665N(L) 65 180 1200 1200 1200D680N(L) 80 300 1200 1200 1200D6100N(L) 100 580 200 200 1200 1) 1200D6125N(L) 125 820 600 2) 1200 1200 1200D6150N(L) 150 1600 600 1200 1200D6200N(L) 200 2900 1200D6250N(L) 250 4400 1200D6300N(L) 300 7300 600 1200D6350N(L) 350 10900 600

    1)GR..A-52)GR..A-7

    Notes for project planning Shut-off and buttery valves for open-close applications

    Denition psClosing pressure at which the actuator can stillseal the valve tightly allowing for the appropriateleakage rate.

    Denitions kvmaxand The ow rate of kvmaxwill ensue when the valve isfully open (90).Zeta is the coefcient for the pressure lossthrough the fully opened valve (90).

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    Notes for project planning Shut-off and buttery valves for open-close applications

    Design and dimensioning (Continued)

    Flow rate buttery valves D6..ND6..NL

    Buttery valve Differential pressure pv100

    Type DN[mm]

    kvmax[m3/h]

    0,01[kPa]

    0,1[kPa]

    1[kPa]

    2[kPa]

    3[kPa]

    D625N 25 45 0.45 1.42 4.50 6.36

    Flow

    100[m3/h]

    D632N 32 55 0.55 1.74 5.50 7.78D640N 40 70 0.70 2.21 7.00 9.90 12.1D650N(L) 50 90 0.90 2.8 9.0 12.7 15.6D665N(L) 65 180 1.80 5.7 18.0 25.5D680N(L) 80 300 3.0 9.5 30 42D6100N(L) 100 580 5.8 18.3 58 82D6125N(L) 125 820 8.2 26 82D6150N(L) 150 1600 16 51 160D6200N(L) 200 2900 29 92 290D6250N(L) 250 4400 44 139 440D6300N(L) 300 7300 73 231 730D6350N(L) 350 10900 109 345 1090

    Pressure drop

    0.1

    0.

    01

    0.

    02

    0.

    03

    0.

    04

    0.

    05

    0.

    06

    0.

    08

    0.2

    0.3

    0.4

    0.5

    0.6

    1

    0.8

    1.5

    2

    3

    4

    5

    6

    10

    8

    20

    30

    40

    50

    60

    100

    80

    200

    300

    400

    500

    600

    1000

    800

    0.

    1

    0.2

    0.3

    0.40.50.6

    0.81 2 3 4 5 6 8

    10

    0.03

    0.06

    0.08

    0.11

    0.140.17

    0.28

    0.22

    0.56

    0.83

    1.1

    1.41.7

    2.8

    2.2

    5.6

    8.3

    11

    1417

    28

    22

    56

    83

    110

    140170

    280

    2201)

    100[l/s]

    pv100[kPa]

    0.0

    001

    0.0

    002

    0.0

    003

    0.0

    004

    0.0

    005

    0.0

    006

    0.0

    008

    0.0

    01

    0.0

    02

    0.0

    03

    0.0

    04

    0.0

    05

    0.0

    06

    0.0

    08

    0.0

    1

    0.0

    2

    0.0

    3

    0.0

    4

    0.0

    5

    0.0

    6

    0.0

    8

    0.1

    pv100[bar]

    100[m

    /h]

    DNk

    vmax

    350

    1090

    0

    250

    4400

    125

    820

    100

    580

    6518

    0

    5090

    300

    7300

    200

    2900

    150

    1600

    8030

    0

    4070

    3255

    2545

    1)

    1)

    Denitions kvmaxand The ow rate of kvmaxwill ensue when the valve isfully open (90).Zeta is the coefcient for the pressure lossthrough the fully opened valve (90).

    Legendpv100 Differential pressure with valve

    completely open100 Nominal flow rate with pv100

    pv1001) The maximum speed in the butterfly

    valves is 4 m/s

    Formula

    =pv100

    100

    100

    kvmax

    2

    pv100 [kPa]100 [m3/h]kvmax [m3/h]

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    Notes for project planning Buttery valves for control mode

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    Project planning

    Relevant information The data, information and limit values listed on the data sheets and mounting instructions D6..are to be taken into account and/or complied with, respectively.

    Pipeline clearances The minimum clearances between the pipelines and the walls and ceilings required for projectplanning depend not only on the valve size but also on the selected actuator.

    Design and dimensioning

    General information Buttery valves can be used in control mode when the following values are complied with: The maximum flow speed of 4 m/s may not be exceeded in the butterfly valve. The butterfly valve is to be designed in such a way that the nominal pipe width corresponds to

    nominal butterfly valve width. The narrowing of the pipe must be designed in such a way thereby

    as to ensure optimum flow in order to ensure that the pressure drop is kept as low as possible.

    Technical data for control mode Differential pressure pv0: 0,3Rangeability: >30

    The S-shaped characteristic curve of the D6..N(L) buttery valve (BFV) does not correspondto the equal percentage characteristic curve pursuant to VDI 2176. It is only in the angle ofrotation range between 0 and 54 that one can speak of an approximately equal percentagecharacteristic curve. For an opening angle of 54, the kvscorresponds to approx. 35 percent ofthe kvmaxvalue for a 90 opening angle.

    S-shaped characteristic curve

    0 18 36 54 72

    kv/kvmax

    100%

    50%

    0%

    90

    kvs 35%

    Scaled characteristic curve range

    10%

    10%

    0%

    0% 100%

    100%

    0%

    54

    kv/kvs

    The kvs@ 54 listed in the differential pressure table deviates from the usual tolerance (10%) forsome nominal widths. The equivalence factor of the equal percentage characteristic curve is ~2.5.

    Flowr

    ate

    Opening angle

    S-shapedcharacteristic curvee.g. D6300N

    Theoreticallyequal-percentagecharacteristic curve

    Deviation >10%

    Deviation >10%

    Denitions kvmaxund kvsThe ow rate of kvmaxwill ensue when the disc isfully open (90).The kvs value refers to the ow rate at 54opening angle, 1 bar pressure loss and medium

    temperature: 5C ... 40C.

    S-shapedcharacteristic curvee.g. D650N

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    Notes for project planning Buttery valves for control mode

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    Design and dimensioning (Continued)

    Because of this fact, there is no conguration option available with the modulating actuators oflimiting the angle of rotation range from 0 to 54.The angle of rotation range required can be adjusted accordingly afterwards with the MF andMP types using the PC-Tool MFT-P, Version 3.3.

    The differential pressure pv@54 (Marked in grey in the table Flow rate) may not be

    exceeded. This will ensure that the maximum permissible medium speed of 4 m/s is maintained.Depending on the nominal width, the closing angle lies between 7 and 16.

    Flow rate Buttery valve

    Type DN[mm]

    kvs@54[m3/h]

    @54[m3/h]

    pv@54[kPa]

    Initial ow angle

    D625N 25 16 2.7 2.9 ~16D632N 32 19 4.3 5.0 ~16D640N 40 25 6.4 6.8 ~13D650N(L) 50 32 9 8.2 ~13D665N(L) 65 63 16 6.6 ~13D680N(L) 80 105 24 5.1 ~13D6100N(L) 100 203 45 4.8 ~10D6125N(L) 125 287 65 5.1 ~10D6150N(L) 150 560 105 3.5 ~10D6200N(L) 200 1015 180 3.1 ~7D6250N(L) 250 1540 281 3.3 ~7D6300N(L) 300 2555 416 2.6 ~7D6350N(L) 350 3815 511 1.8 ~7

    Closing pressure Buttery valve Actuators

    SR..A SR..P GR..A DGR..A DR.. SY2 SY3 SY4 SY5

    Type DN[mm]

    ps[kPa]

    ps[kPa]

    ps[kPa]

    ps[kPa]

    ps[kPa]

    ps[kPa]

    ps[kPa]

    ps[kPa]

    ps[kPa]

    D625N 25 1200 1200D632N 32 1200 1200D640N 40 1200 1200D650N(L) 50 1200 1200D665N(L) 65 1200 1200D680N(L) 80 1200 1200D6100N(L) 100 200 1200 1)

    D6125N(L) 125 600 2) 1200 1200 1200D6150N(L) 150 600 1200 1200D6200N(L) 200 1200D6250N(L) 250 1200D6300N(L) 300 600 1200D6350N(L) 350 600

    1)

    GR..A-52)GR..A-7

    FormulaThe effective volumetric ow calculated foropening angle is:

    @ = kvs@ pv@

    100

    100@ [m3/h]kvs@ [m3/h]p@ [kPa]

    Denition psClosing pressure at which the actuator can stillseal the valve tightly allowing for the appropriateleakage rate.

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    Notes for project planning

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    Notes for project planning

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    Notes for project planning

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