"> SWEP SWEP B12 200kW LO cooling
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SWEP

SWEP B12 200kW LO cooling

SWEP SWEP B12 200kW LO cooling — Heat Exchangers, LO cooling.

Inspector Detail

Common issues

  • Internal fouling from lube oil degradation products/varnish restricting flow and reducing heat transfer
  • Cross-contamination between circuits following an internal braze/plate failure
  • External corrosion at connections and nozzles, particularly with dissimilar-metal contact
  • Reduced LO cooling capacity from partial blockage of the narrow plate channels
  • Fatigue cracking of brazed joints from thermal cycling or pressure pulsation
  • External fouling or scale build-up on the coolant-side if seawater or untreated fresh water is used
  • Vibration-induced fatigue at pipework connections

Inspection checklist

  • Check differential pressure across the LO side against the commissioning baseline
  • Monitor outlet temperature/approach temperature against design to detect performance degradation
  • Inspect the external shell and connections for oil weepage indicating an internal leak
  • Check for external corrosion, especially at brazed end connections and mounting brackets
  • Verify any fitted insulation is intact and not trapping moisture against the shell
  • Check mounting/support brackets for vibration-related fatigue cracks
  • Sample oil for coolant contamination if an internal leak is suspected
  • Confirm associated pressure relief/safety devices are functional

Service intervals

Chemical (CIP) cleaning condition-based, typically every 1-3 years depending on oil condition and duty
Differential pressure trend check monthly to quarterly as part of routine monitoring
Full performance/thermal efficiency check annual
External visual inspection every 3-6 months or per the PMS

Typical wear limits

Differential pressure across the unit (fouling indicator) flag for cleaning once DP rises noticeably above the commissioning baseline - as a general guide often in the order of 1.5-2x clean condition, confirm against the original design DP
Thermal approach temperature an increase of more than a few degrees C above the design approach typically indicates fouling or reduced performance - compare against commissioning data
External connection wall condition assess by visual/thickness check against original nozzle wall thickness - no universal numeric limit, follow the class thickness-gauging criteria applied to the associated piping

Ranges are typical for this design class. Always confirm against the manufacturer documentation for your serial number.

Critical spares

  • Complete replacement unit - brazed plate exchangers are fully sealed and cannot be reopened or re-plated in the field
  • Gaskets/O-rings at pipe connections (flanged or threaded joints only, none internal)
  • Isolation valves and associated pipe fittings
  • Temperature and pressure sensors fitted to the circuit
  • Mounting/support bracket hardware

Safety

  • Hot surfaces on the LO-side piping and connections - burn hazard
  • Pressurised system - isolate and depressurise fully before disconnecting any joint
  • Risk of oil mist or spray if a connection is broken under residual pressure
  • Confined space considerations if the unit is mounted in a tight engine room location

Class survey

Where part of a class-surveyed cooling system, typically falls under Continuous Survey Machinery. Class looks for pressure testing history, a fouling-related cleaning routine in the PMS, and evidence of leak-free operation. No internal survey is possible on a brazed unit - assessment relies on performance trending and external inspection.

Estimated lifetime: Not conventionally rated in running hours since there are no moving parts. Brazed plate heat exchangers of this class typically give 15-25 years of service if kept within design pressure/temperature and fouling is controlled.

Components & Design

Component data being added…

Technical Data

hx type brazed_plate_heat_exchanger
capacity kw 200
material stainless_steel_316

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Equipment Model #78984 · ✓ still in production