Flash Steam from steam trap
Flash Steam from steam trap
(OP)
There are two outlet from steam traps " liquid condensate and the Flash Steam that its going to air"
the liquid condensate recover and reuse as feed in our boiler .
But i want to ask , how i can reuse and take the benefit of flash steam that its going to air ?
* boiler capacity 30 Ton/ hr , 16 bar
Thanks
the liquid condensate recover and reuse as feed in our boiler .
But i want to ask , how i can reuse and take the benefit of flash steam that its going to air ?
* boiler capacity 30 Ton/ hr , 16 bar
Thanks





RE: Flash Steam from steam trap
Katmar Software - AioFlo Pipe Hydraulics
http://katmarsoftware.com
"An undefined problem has an infinite number of solutions"
RE: Flash Steam from steam trap
RE: Flash Steam from steam trap
The economics of an energy recovery project aimed at reducing steam usage, or increasing recovery of steam, can easily be oversimplified. Say you're looking to optimize a low-pressure steam system, and let's say that all of that steam originates from a 600# system let-down control valve. The cost (value) of that steam is relatively high. Now consider another case in which that low-pressure steam originates from a 600# system, but in this case the low-pressure steam is the exhaust of a steam turbine (driven by the 600# steam). In this case the value of that low-pressure steam is relatively low.
For a large integrated plant (refinery or chemical plant), the economic analysis of energy recovery projects is surprisingly complex. Accurately determining the value of different levels of steam is the complex part. If a facility doesn't have a reliable steam valuation model, it's easy to be fooled into thinking that there's justification for recovering vented steam, when in reality the most economical option is to vent it to the atm.