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WHY DO WE USE STEAM?
Jonathan Beresford BSc (Hons)
MSc
AKVO Ltd
07773 335812
WHY USE STEAM
 Higher heat content than hot water
– @100psi steam = 2800 kj/kg
– @100psi hot water = 720 kj/kg

 Means smaller pipes can be used
 Means lower flow rates
 Means less weight needs to be supported
BUT
 We need a condensate return system
WHY BOTHER TO RETURN THE
CONDENSATE
 It is very hot
– @15psi hot water contains 500kj/kg
– @90 deg C hot water contains 380kj/kg
– @10 deg C raw water contains 40kj/kg

 It is almost pure
– Reduces blowdown
 Saves energy

– Reduces chemical needs
 Lowers oxygen content

– Minimises water costs
CONDENSTAE SYSTEM
COMPONENTS
 Steam traps
–
–
–
–







Thermostaic
Ball float
Thermodynamic
Liquid expansion

Sight glasses
Strainers
Air vents
Receivers
Pumps
LIQUID EXPANSION TRAP
 Contains an oil filled
element to operate at
preset temperature
 Operates between 60
– 100 deg C
 Must be installed with
condensate discharge
upright.
BALANCE PRESSURE TRAP
 Can be installed
horizontally or
vertically
FLOAT TRAP
 Maximum pressure
230psi
 Should be fitted as
close as possible to
the item of plant
requiring trapping.
 Very effective at
removing high loads of
condensate under start
up conditions
FLOAT TRAP WITH AIR VENT
 Used where steam
locking may be a
problem.
INVERTED BUCKET TRAP
 Designed for
installation in vertical
pipe work
BI-METAL STEAM TRAP
 Can be installed
vertically or
horizontally.
 Can be of a more
complex design
 Installed where precooling of the
condensate is required
prior to discharge.
STRAINERS
•Designed to remove
particulates ahead of
steam traps.
•Must be cleaned out
regularly.
•Available in a range of
materials.
RECOVERY
•Collects condensate
from traps.
•Automatic pump
operation.
•Returns condensate
to hotwell at low
pressure.

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Akvo why do we use steam

  • 1. WHY DO WE USE STEAM? Jonathan Beresford BSc (Hons) MSc AKVO Ltd 07773 335812
  • 2. WHY USE STEAM  Higher heat content than hot water – @100psi steam = 2800 kj/kg – @100psi hot water = 720 kj/kg  Means smaller pipes can be used  Means lower flow rates  Means less weight needs to be supported BUT  We need a condensate return system
  • 3. WHY BOTHER TO RETURN THE CONDENSATE  It is very hot – @15psi hot water contains 500kj/kg – @90 deg C hot water contains 380kj/kg – @10 deg C raw water contains 40kj/kg  It is almost pure – Reduces blowdown  Saves energy – Reduces chemical needs  Lowers oxygen content – Minimises water costs
  • 4. CONDENSTAE SYSTEM COMPONENTS  Steam traps – – – –      Thermostaic Ball float Thermodynamic Liquid expansion Sight glasses Strainers Air vents Receivers Pumps
  • 5. LIQUID EXPANSION TRAP  Contains an oil filled element to operate at preset temperature  Operates between 60 – 100 deg C  Must be installed with condensate discharge upright.
  • 6. BALANCE PRESSURE TRAP  Can be installed horizontally or vertically
  • 7. FLOAT TRAP  Maximum pressure 230psi  Should be fitted as close as possible to the item of plant requiring trapping.  Very effective at removing high loads of condensate under start up conditions
  • 8. FLOAT TRAP WITH AIR VENT  Used where steam locking may be a problem.
  • 9. INVERTED BUCKET TRAP  Designed for installation in vertical pipe work
  • 10. BI-METAL STEAM TRAP  Can be installed vertically or horizontally.  Can be of a more complex design  Installed where precooling of the condensate is required prior to discharge.
  • 11. STRAINERS •Designed to remove particulates ahead of steam traps. •Must be cleaned out regularly. •Available in a range of materials.
  • 12. RECOVERY •Collects condensate from traps. •Automatic pump operation. •Returns condensate to hotwell at low pressure.