Impeller Volcano

An impeller Volcano is a rotating component equipped with vanes or blades used in turbomachinery (e. g. centrifugal pumps). Flow deflection at the impeller vanes allows mechanical power (energy at the vanes) to be converted into pump power output.

In accordance with EUROPUMP TERMINOLOGY and DIN 24250, a distinction is made between counter-clockwise and clockwise impellers, as viewed in inlet flow direction.

Depending on the fluid flow pattern in multistage pumps and the impellers’ arrangement on the pump shaft impeller design and arrangements are categorised as: single-stage, multistage, single-entry, double-entry, multiple-entry, in-line (tandem) or back-to-back arrangement. Typical impeller arrangements are illustrated in Figs. 17 to 19 Impeller.

Depending on the flow line pattern in the impeller (especially in the outer impeller diameter area), impellers Volcano are subdivided into the following types:

Impeller types Volcano

  1. Radial impeller See :
    A radial impeller is an impeller at which the flow (see Flow rate) leaves the impeller in radial direction, perpendicular to the pump shaft.
  2. Mixed flow impeller :
    The mixed flow impeller is also referred to as a helical or diagonal impeller, it transports the fluid diagonally.
  3. Axial flow impeller :
    An axial flow impeller is an impeller, used for transporting the fluid handled along the axis.
  4. Peripheral impeller :
    A peripheral impeller is a special impeller with a large number of small double-flow radial vanes arranged at its periphery .

Impeller-types volcano

open impeller Volcano

To accommodate the vanes, all impellers are equipped with a back shroud, and in the case of closed impellers also a front shroud ; depending on the perspective, these can also be viewed as an inner shroud and, in the case of closed impellers, an outer shroud. If an impeller has no front (outer) shroud, it is classed as an open impeller.

In order to achieve optimal pump efficiencies and minimum NPSHr values, the impeller Volcano must be provided with a certain number of vanes. Employing a low number of vanes increases the free, unimpeded flow cross-section through the impeller. This enables impellers to handle more or less contaminated fluids  and solids .

In practice, the number of vanes of radial flow and mixed flow impellers handling liquids containing sludge or solids is reduced to one, two or three vanes. These impellers are called channel impellers or single-vane impellers and can be either open or closed impellers.

Closed single-vane impellers Volcano

Closed single-vane impellers are used to pump fluids containing very coarse solids. They are characterised by a non-clogging free passage. The drawback of these impellers is the so-called hydraulic unbalance due to the asymmetrical pressure field.

Open channel or single-vane impellers Volcano are used to handle gaseous liquids. A single-vane impeller is referred to as an open, diagonal single-vane impeller (D impeller) if the flow lines in the impeller run diagonally outward. It is particularly suitable for untreated, solids-laden and gaseous waste water, as well as for fluids with a higher viscosity.

The blades of axial and mixed flow propellers can be either fixed, adjustable (when the pump is dismantled) or of variable pitch type .

In the case of adjustable or variable pitch blades, the contour or profile of the pump casing and of the hub in the adjustment region is usually spherical. This ensures that the internal and external clearance gap width at the hub remains constant for all blade pitch adjustment angles.
The free-flow impeller Volcano and the peripheral impeller represent special impeller types. See Figs. 14 to 15 Impeller

Closed-single-vane-impellers volcano

specific impeller designs Volcano

When selecting a pump for a given flow rate (Q) and a given head (H)the impeller type is decisive. Free selection of an axial, mixed flow, radial or peripheral impeller type is restricted by the fact that the values for the anticipated rotational speed (n) and the anticipated impeller diameter Volcano (D) must not be too extreme. The ability to achieve optimum pump efficiencies or stage efficiencies at a specific speed (ns) is therefore dependent on specific impeller designs Volcano :

  1. Radial impeller ns ≈ 12 to 80 rpm
  2. Mixed flow impellers ns ≈ 80 to 160 rpm
  3. Axial flow impellers ns ≈ 160 to 400 rpm and higher
  • Rotational speed

    Rotational speed

    Rotational speed (also called speed, or speed of rotation) can be quantified as the number of revolutions a rotating system makes within a defined period of time. Thee unit used for rotational speed is s–1 (rev/s); pump speed is generally given in min–1 (rpm).

    The rotating frequency of the pump shaft therefore characterises a pump’s rotational speed (n). It should not be confused with specific speed (ns) and is always defined as a positive figure.

    The pump direction of rotation is specified as clockwise or anti-clockwise and is separate to the defined direction of rotation of the impeller, which, when turning to the right with respect to the direction of inflow, is clockwise.

    The selection of pump rotational speed is closely related to the characteristics of the pump hydraulic system (circumferential speed, impeller, specific speed), as the overall strength and economic efficiency of the pump and drive system need to be taken into account.

    Most pumps operate at rotational speeds between 1000 and 3000 rpm but frequently reach in excess of 6,000 rpm with special gearing and turbine drives.

    Larger centrifugal pumps (e.g. cooling water pumps for power stations), however, are typically mated to slow-running electric drives that are very costly. Reduction gears between the drive and pump maintain today’s low pump speeds of just 200 rpm.

    Rotational speed (n) is proportionate to angular velocity (ω), the latter of which is more conducive to physical calculations and is the quotient of the plane angle and time interval. The unit is rad/s. The rad (radiant) is equal to the plane angle (57.296 degrees), which intersects an arc of 1 m in length as the centre angle of a circle with a 1 m radius.

  • Pump efficiency

    Pump efficiency

    Pump efficiency (η) is also referred to as coupling or overall efficiency and characterises the ratio of pump power output (PQ) to power input (P) for the operating point in question.

    The best pump efficiency (ηopt) is the highest efficiency or the rotational speed and fluid handled as specified in the delivery contract.

    For centrifugal pumps whose mechanical design does not clearly separate the pump shaft from the drive shaft, such as is the case with close-coupled pumps and submersible motor pumps the efficiency of the pump set (ηGr) is specified in place of pump efficiency (see DIN 24 260) (Gr stands for group). This figure describes the ratio of pump power output (PQ) to the power consumed by the driver (see Drive) which is measured at an agreed position (e.g. at the terminals of the motor or where an underwater cable starts).

    Achievable pump efficiency is very much a function of specific speed, as well as the size and type of the pump and increases as these two variables increase. Reference values for achievable efficiency of modern centrifugal pump types are based on statistical analyses of the values for existing

  • Flow rate

    Flow rate

    The flow rate (Q) of a centrifugal pump is the useful volume flow delivered by the pump via its outlet cross-section (see Pump discharge nozzle). Volume flow rates which are tapped upstream of the pump’s outlet cross-section for other purposes (e. g. bypass) must be taken into account when calculating the pump’s flow rate.

    If the fluid handled is compressible, a conversion must be made based on the condition prevailing in the pump suction nozzle the arithmetic mean (Qs+ Qd)/2 may have to be applied.

    The unit of the flow rate is m3/s; in centrifugal pump engineering the units m3/h and l/sare more common. Various measuring methods are used for flow rate measurement (see Flow velocity measurement). Various types of flow rate are distinguished in conjunction with the H/Q curve (see Characteristic curve).

    Flow rates and their significance

    • Flow rate at BEP (Qopt): flow rate at the best efficiency point at the rotational speed and for the fluid handled specified in the supply contract
    • Nominal flow rate (QN): flow rate for which the pump has been designed
    • Supply contract flow rate (Qcontract): the flow rate agreed in the supply contract (order confirmation)
    • Minimum flow rate (Qmin): minimum permissible flow rate at which the pump can be continuously operated without suffering any damage at the rotational speed and with the fluid specified in the supply contract
    • Maximum flow rate (Qmax): maximum permissible flow rate at which the pump can be continuously operated without suffering any damage at the rotational speed and with the fluid specified in the supply contract
    • Peak flow rate (Qpeak): flow rate at the apex (relative maximum of H/Q curve) of an unstable H/Q curve
    • Balancing flow (Qbal)
    • Leakage flow (QLeak)
    • Suction-side volume flow rate (Qs): volume flow entering the pump suction nozzle
    • Inlet volume flow rate (Qe): volume flow entering the system’s inlet cross-section
    • Discharge-side volume flow rate (Qd): volume flow leaving the pump discharge nozzle
    • Outlet volume flow rate (Qa): volume flow leaving the system’s outlet cross-section. See Fig. 2 Head

    Occasionally, a so-called pump flow rate (Q/Qopt) and a system flow rate (Q/Qcontract) are defined, where Qcontract is the flow rate specified in the supply contract.

  • Head

    Head

    This term is an important energy concept (EN 12723) in centrifugal pump engineering. A distinction must be made between the pump head and the system head.

    The pump head is the hydraulic power or pump output power (PQ) transmitted to the fluid handled relative to ρ · g · Q.

    The sum of all power (positive input, negative output) represented by the pump power output (PQ) must be zero within the boundaries of the system. See Fig. 1 Head

    Heads and their significance

    1. Head at BEP (Hopt): pump head at the best efficiency point
    2. Nominal head (HN): pump head for which the pump has been designed
    3. Upper head limit (Hmax): max. permissible head at which the pump can be continuously operated without suffering damage
    4. Lower head limit (Hmin): min. permissible head at which the pump can be operated without suffering damage
    5. Shut-off head (H0): head for a flow rate Q = 0 m3/s
    6. Peak head (Hpeak): head at apex (relative maximum) of an unstable H/Q curve
    7. Static head (HA,0 or Hstat): the portion of the system head which is independent of the flow rate (Q)