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Description:
Condensate released from process at high pressure has a tendency to vaporize due to pressure drop. This possibility leads to water hammer in condensate lines leading to a dirty and high – loss condensate network. Flash Vessels are recommended for collecting high pressure condensate before it is returned to boiler feed water circuit.
Available sized and pipe Connections:
|
Size |
Condensate Inlet |
Condensate Outlet |
Flash Steam Outlet |
|
6 |
80 NB FLG TAB ‘F’ |
50 NB FLG TAB ‘F’ |
80 NB FLG TAB ‘F’ |
|
8 |
80 NB FLG TAB ‘F’ |
50 NB FLG TAB ‘F’ |
80 NB FLG TAB ‘F’ |
|
12 |
80 NB FLG TAB ‘F’ |
50 NB FLG TAB ‘F’ |
80 NB FLG TAB ‘F’ |
|
16 |
150 NB FLG TAB ‘F’ |
50 NB FLG TAB ‘F’ |
125 NB FLG TAB ‘F’ |
|
18 |
150 NB FLG TAB ‘F’ |
50 NB FLG TAB ‘F’ |
125 NB FLG TAB ‘F’ |
Drain: Provided at the bottom 1 “BSP
Limiting Conditions
Maximum working Pressure = 10.5 kg/cm2
Maximum working Temperature = 1800C
Cold hydraulic test pressure = 21.0 kg/cm2
Installations
The flash vessel should be mounted with the flash steam outlet at the top
Material No. Description Material Standard
1. Main Shell Carbon Steel IS 2062
Features of UKL Flash Vessels
UKL Flash Vessel is an excellent tool for energy conservation. Under different operating parameters UKL Flash vessel pays back for it’s cost in less than 45 days.
High pressure condensate will release as much as 10-15% of LP steam that can be put back into process loop for substantial monetary gains.
The UKL Flash vessel is generously sized to ensure low flow velocities that help easy separation of released steam form the condensate.
A safety valve provided on the flash vessel will ensure safety of the equipment where this LP steam is proposed to be used.
A check valve if fitted at the outlet of flash steam will ensure preventing any back pressure that may cause in the event HP condensate is not generated in the process.