Pump type BB1– According to API 610

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Design:

  • Horizontal, axially split, one-and two stage between bearings
  • Double suction impeller
  • Single or double volute, depending on size
  • Diffuser or overflow piece after first stage for two stage execution
  • Driving from both sides possible
  • Mechanical seals (single, double, tandem)
  • Oil lubricated rolling bearings with rotor located by the non drive end for residual hydraulic axial thrust from hydraulically balanced impeller
  • Radial as well as axial loads can be also taken by oil lubricated bearings
Description
  • Oil and Gas
  • Petrochemical
  • Steel complex and mining
  • Power Plant

Product features

Features:

  • Low NPSH required in case of double suction impeller
  • Suction and discharge nozzles in botoon half of the casing

 

Type of bearingRolling element and plain bearings
Casing partitionAxially split
Drive frequency50 Hz /60 Hz
Type of driveElectric motor
Drive voltageLow voltage, high voltage
No. of impeller entriesDouble entry
Type of installationLong-coupled
Type of couplingDirect; Gear
Type of lubricationgrease-/oil- and product lubrication
Max. permissible fluid temperature200 °C
Min. permissible fluid temperature-45 °C
Nozzle positionIn-line
Pump set locationDry installed
Suction characteristicsNon-priming
Type of casingVolute casing
Type of impellerRadial; Closed
Type of connectionFlange
Maximum headUp to 800 m per stage
Installation positionHorizontal or vertical
Shaft seal typeGland packing; Mechanical seal
Main applicationsEnergy; Industry and process engineering; Mining / Dredges
Casing materialCast iron; Nodular cast iron; Cast duplex steel; Ni-Resist
Maximum discharge-side pressure150 bar
Maximum drive rating3300 kW
Type of installationStationary
Maximum flow rate15000 m³/h
Minimum flow rate1200 m³/h
Maximum speed of rotation1800 1/min

 

Usages:

Applications:
Pumping of:

  • crude oil
  • petroleum products

Exploitation:

  • pipeline
  • offshore industry
  • fire fighting services

Advantages:

  • Branches on bottom half of the casing, therefore the pipe works do not have to be disturbed for inspection (overhaul)
  • Short inspection time
  • Wide choice of hydraulics
  • Possibility to install different impellers in exiting casing (especially valid for one stage pumps) – improving the economy of the installation
  • Reduced radial thrust and bearings loads
  • Reduced shaft deflection at seals
  • Interchangeable wearing parts
  • NPSH, efficiency and casing stiffness better as OH1 and OH2
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