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Our technology. Your success. Pumps n Valves n Service KSB Know-how: Supplementary Planning Information for Amacan Pumps

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  • Our technology. Your success.Pumps n Valves n Service

    KSB Know-how: Supplementary Planning Information for Amacan Pumps

  • 02

    The know-how volumes can easily be downloaded or

    ordered here: www.ksb.de/know-how

  • 03

    Page

    Contents

    04 Supplementary Planning Information for Amacan Pumps

    04 Calculation of support rope length

    06 Cable assembly variants

    07 Fitting of cable assembly

    07 Venting of discharge tube

    11 Cable entry at discharge tube

    12 Cable holder in discharge tube

    13 Detailed views of cable assembly variants

  • 04

    Supplementary Planning Information for Amacan Pumps

    Calculation of support rope length

    The support rope length is determined by the installation

    conditions and the size of the Amacan pump.

    Dimension “L” is always required to determine the correct

    length of the support rope.

    “L” is the dimension from the lower edge of the discharge tube

    to the attachment point on the discharge tube cover, discharge

    tube wall or cross bar in the case of an open discharge tube.

    Dimension h2 or h4 is determined by the pump size.

    The total cable length Lstotal results from the difference

    between dimension “L” and h2 or h4 respectively.

    The on-site lifting height of the lifting equipment or hoist must

    be taken into account when designing the cable assembly.

    NOTE:

    The lifting height of the hoist must be higher than the total

    pump height. If the lifting height is restricted by the building or

    the lifting height of the hoist, additional lifting lugs can be

    integrated in the support rope to allow the pump to be attached

    to a second hoist.

    If additional lifting lugs are fitted, two hoists are required.

    Fig. 1: Amacan K

    Supplementary Planning Information for Amacan Pumps

    Lstotal

    h4

    L

    Lower edge of discharge tube

    Fig. 2: Amacan P / S

    h2

    L

    Lower edge of discharge tube = lower edge of pump

    Lstotal

  • 05

    Additional lifting lugs allow the support rope including cables

    and pump to be attached to a second hoist after the pump has

    been partially lifted by the first hoist.

    The hoist can continue lifting until the next maximum lifting

    height is reached.

    This process is repeated until the lifting or installation procedure

    is completed.

    Fig. 2a = Lifting and positioning the pump set

    1 = Lifting rope

    2 = Hoist (1)

    3 = Lifting accessories (crane hook)

    4 = Lifting equipment trolley or hoist 2

    5 = Support rope

    6 = Free lifting lug

    Fig. 2b / 2c = Securing control and power cables

    Fig. 2d / 2e = Lowering the pump set

    Fig. 2a

    Fig. 2b | 2c

    Fig. 2d | 2e

    1

    2 34

    56

  • 06

    Minimum lengths must be observed for individual rope sections.

    Specifications regarding rope lengths and technical feasibility

    depending on rope diameter are made by the rope manufacturer.

    The rope diameter is determined by the weight of the pump set.

    The optimum number of lifting lugs should be selected based on

    technical considerations. As the lifting height of the lifting

    equipment must be at least as high as pump length h1, individual

    rope sections only need to be this length.

    Each additional lifting lug requires additional work and time for

    installation on site.

    If dimension Lstotal is > 5 m, we recommend using rope spacers

    (supports). This is necessary to rule out any possibility of the

    support rope incl. cables hitting the discharge tube, and causing

    damage.

    Cable assembly variants

    a = Basic design

    b = Design with lifting lug (59-47)

    c = Design with lifting lug and support (59-47 and 59-7)

    a b c

    Supplementary Planning Information for Amacan Pumps

  • 07

    Fitting the cable assembly

    When fitting the cable assembly (support rope and control/

    power cables), always start at the pump and continue in the

    direction of the upper end of the discharge tube. Ensure that the

    cables are fitted with a sufficient degree of flexibility to prevent

    damage to the cable entries during inspections or repairs.

    The installation steps must be carried out carefully (see operating

    manual) and only using original KSB parts, otherwise there is a

    risk of cable damage.

    During this work it is also important to observe the permissible

    bending radii in relation to the respective cable diameter.

    Bending radii for free movement:

    Up to a cable diameter of 12 mm: 4 times the outside cable

    diameter

    For cable diameters larger than 12 mm: 5 times the outside

    cable diameter

    Components that come into mechanical contact with the cables

    or cable insulation must be checked for sharp corners and edges

    and, if necessary, deburred or reworked (filing or grinding).

    Venting of discharge tube

    Venting the discharge tube is vital for various hydraulic reasons.

    It is possible to calculate the size of the air volume and then

    determine the size of the cross-sections for the required venting

    devices.

    The above depends on the discharge tube’s geometry and the

    pipe connected to the discharge tube. The system is completely

    filled with air to begin with. When the pump starts pumping, the

    discharge tube and the connected pipe fill with water. Depending

    on the flow velocity in the individual system sections, the air is

    entrained or trapped in certain areas and compressed.

    The compressed air volume (air cushion) leads to transient or

    unsteady pump operating behaviour and influences the H/Q

    characteristic curve. As a result, the pump does not operate at

    the calculated design point under steady-state operating

    conditions. This operating behaviour also places additional loads

    on mechanical components and shaft seals.

    If air cushions form, i.e. air is trapped, and block e.g. flow

    cross-sections, this will also change the operating point. The

    friction losses in the piping will increase, causing the pump to be

    pushed towards the part load range.

    This will significantly increase the input power required by the

    hydraulic system and might lead to motor overload. The further

    away the operating point from the best efficiency point, the

    more likely it is that mechanical vibrations and hydraulic

    fluctuations will occur. Noise emissions and recirculation can

    occur on the left-hand side of the smallest permissible

    continuous operating range.

  • 08

    Discharge tubes and the connected piping should therefore be

    assessed with regard to potential air cushions and fitted with

    appropriate venting devices.

    The uncompressed air volume can be roughly determined based

    on the following information: the pump size and thus the

    discharge tube diameter, the overall discharge tube length and

    the position of the discharge nozzle branching off into the

    horizontal pipe. Two options are available for venting: either a

    continuous process using a vent pipe/vent hose or a temporary

    process using an air valve. If a vent pipe/vent hose is used, it

    should end above the max. water level in the pump sump. The

    venting devices (vent pipe/vent hose and air valve) must be

    attached in the pump sump in such a way that they can also

    serve to remove fluid from both the pump and the piping after

    pump start-up (fluid via the pipes, a water/air mixture or spray

    via the air valve). Contamination is thus avoided, ensuring

    compliance with occupational health and safety regulations.

    If the installation depth of the discharge tube is more than 10 m,

    the conditions in the system should be examined. This is done

    using modelling, i.e. a process for analysing transient conditions

    (also applied for pressure surge calculation). On the basis of this

    analysis, it is possible to determine the starting and stopping

    behaviour including the resultant conditions in the system and, if

    necessary, the behaviour of the check valve in order to avoid

    extreme valve closures.

    In addition to this information, backflow into the pump sump

    can also be assessed.

    In particular, pumps with high specific speeds (ns > 120 rpm)

    tend to exceed the speed in reverse operation (turbine mode).

    Vent line

    Pump size

    Amacan P Amacan K Amacan S

    G 1/2 500

    G 1/2 600

    G 1/2 650

    G 3/4 700 700

    G 1 800 800 800

    G 1 850

    G 1 900 900

    G 1 1/4 1000 1000 1000

    G 1 1/2 1200 1200

    G 1 1/2 1300

    G 2 1500

    G 2 1600

    Table 1: Recommended cross-sections for vent lines

    Supplementary Planning Information for Amacan Pumps

  • 09

    This reverse operating mode can lead to mechanical damage to

    the impeller and also to the bearings. A further aspect to be

    considered is pump re-start. In the worst case scenario, the

    pump and motor would still be rotating in turbine mode while

    the machine receives the signal to re-start the pump.

    Vent line

    Fig. 3: Discharge tube with vent line

    Fig. 4: Discharge tube with air valve

    Air valve

  • 10 Supplementary Planning Information for Amacan Pumps

    Fig. 5: Throttled-operation curve (pump characteristic curve) with positive speeds | Torque with positive speeds | Throttled-operation curve (turbine characteristic curve) with negative speeds

    Fig. 6: Complete characteristic curve of a pump with mixed flow impeller; ηα = 145

    +H

    /H*

    n/n*=+125%

    200%

    %-100

    100

    -200 % -100 100 % 200

    +100

    +75

    +50+25

    AB

    G

    H

    +Q/Q*

    M=0

    a

    +Q/Q*

    G

    A

    H

    B

    %-100

    200%

    +M

    /M*

    C

    D

    E

    % -100 100 % 200

    +100

    +75

    +50

    +25

    +125

    -M/M

    *

    -100-75-50

    -25F

    H=0

    100

    H=0

    b c

    M=

    0

    +H

    /H*

    200%

    D

    CE

    F

    +Q/Q*

    %-100

    -200 % -100 100 % 200

    100

    0

    -125-100-75-50-250

    G

    A

    B

    C

    D

    F

    E

    +n

    /n*

    M=0

    M=+

    100

    H=+100

    %

    +Q/Q*

    %-100

    +75+50

    +30

    +10

    +200

    +150

    +250

    H=-

    100%

    +75+5

    0

    +30 +1

    0

    +200

    +150+2

    50

    H=+1

    00

    +75 +

    50 +30

    +10

    -100%

    +100

    +75+50

    +30

    +10

    +200+150

    +250

    M=-10

    0-75

    -50

    -30

    -10

    -200

    -150

    -250

    H=0

    -200

    -75-50-30-10

    -200-150

    -250

    Q=

    0

    H=0

    M=0

    H=0

    M=0

    n=0G

    A

    B

    C

    DF

    E

    H

    -Q+H+M-η

    -Q+H-M-η

    -Q-H-M-η

    +Q-H-M-η

    +Q-H-M+η

    +Q-H+M+η

    +Q+H+M+η

    -Q+H+M+η

    -Q

    -Q+H+M-η

    -Q-H-M-η

    +Q-H-M-η

    +Q-H-M+η

    +Q+H+M+η

    -Q+H+M+η

    -Q

    +Q

    -η+η

    +n

    /n*

    +Q/Q*

    G

    A

    B

    C

    F

    E

    -100% 100%

    -200%

    -100

    100

    H=+100

    %

    +75+50+30

    +10

    +200

    +150

    +250

    M=+10

    0

    M=0

    H=0

    M=0

    H=0

    +75

    +50+30+10

    +200

    +150

    +250

    M=-10

    0-75-50

    -30

    -10

    -200-15

    0

    -250

    H=-10

    0%-75-50

    -30-10

    -200-15

    0

    -250

    +Q

    H=0

    M=0

    H=0M

    =0

    G

    A

    B

    C

    D FE

    H

    n=0

    -η+η

    Fig. 7: Complete characteristic curve of an axial flow pump; ηα = 260

  • 11

    Cable entry into discharge tube

    Split cover variants are only recommended to a limited extent as

    leakages can occur at the joint between the two cover parts.

    Variants using gland packings as sealing elements make

    installation more complicated. If gland packings are used, they

    should preferably be installed in a horizontal position as

    recommended by the gland packing manufacturer.

    Fig. 8: The design with welding sleeves is the variant recommended by KSB.

    Fig. 9: Design variant with transit frame (up to 1 bar) (split cover)

    A

    A

    A-A

    1

    5

    6

    2

    36

    A-A

    4

    7

    6

    5

    4

    Key:

    1 = Discharge tube cover2 = Manhole cover3 = Welding sleeve4 = Threaded bush with cable entry to DIN 224195 = Eye plate for fastening the cable support (support rope)6 = Gasket

    Key:

    1 = Discharge tube cover2 = Transit frame3 = Packing and insert blocks4 = Cover segment with cable gland5 = Closed-cell profile seal in groove between the two cover parts6 = Sealing arrangement of groove between the two cover parts7 = Support brackets for cover segment with cable glands8 = Gasket (e.g. rubber with fabric reinforcement)

    1

    23

    8

  • 12

    Fig. 10: Cross bar on the open discharge tube or in the building

    Fig. 11: Cable support sleeve for additional strain relief

    2 1

    3

    Key:

    1 = Holder2 = Rail / support3 = Lifting lug for holder (rope)

    Key:

    1 = Cable entry to DIN 224192 = Threaded bush3 = Welding sleeve4 = Shackle5 = Cable support sleeve

    1

    2

    3

    4

    5

    Supplementary Planning Information for Amacan Pumps

    Cable holder in discharge tube

    Cable support sleeve for additional strain relief if long cable

    sections with large cable cross-sections are used or if dimension

    Lstotal is very small and an appropriate rope cannot be

    manufactured for technical reasons.

  • 13

    Lsto

    tal

    L S

    l 1

    5050

    59-8

    59-1

    7.02

    59-4

    772

    059

    -24

    733.

    05

    719.

    0559

    -17.

    01

    Detailed view

    l 1l 1

    = 3

    00 ..

    . 400

    Legende:

    A = Basic design 59-8 = Turnbuckle59-17 = Shackle59-24 = Rope720 = Fitting 733.05 = Hose clip 719.05 = Hose

  • 14 Detailed view

    l 1 =

    300

    ... 4

    0050

    50l 1

    5050

    AB

    59-8

    59-1

    7.02

    59-4

    759

    -47

    59-1

    7.01

    720

    59-2

    473

    3.05

    719.

    05

    L to

    tal

    L S

    Key:

    B = Design with lifting lug (59-47) 59-8 = Turnbuckle59-17 = Shackle59-24 = Rope720 = Fitting733.05 = Hose clip 719.05 = Hose On ropes with additional lifting lugs, the individual ropes (L1=L2) are always the same length

    L 1L 2

  • 15

    A

    59-8

    59-1

    7.02

    59-4

    772

    073

    3.05

    719.

    0559

    -47

    59-1

    7.01

    A

    50

    Key:

    C = Ausführung mit Tragöse und Stützkörper (59-47 und 59-7) 59-8 = Turnbuckle59-17 = Shackle59-24 = Rope720 = Fitting733.05 = Hose clip 719.05 = HoseOn ropes with additional lifting lugs, the individual ropes (L1=L2) are always the same length

    5050

    50l 1

    l 1 =

    300

    ... 4

    00l 1

    LSto

    tal

    L S

    59-2

    4

    L 2L 1

    59-7

  • 1578

    .026

    /01-

    EN /

    11.1

    9 / ©

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    & C

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