Dears.
Actually, I am recoverying steam in a pressure scrubber from backsteam refiners (wood chips refiners).
Some amount of steam recovered is going to chips heating tank. I am controlling pressure steam at 3 barg and pressure valve is opening
50-60%, means 3-4 ton/hr of steam is going to atm, rest is going to chips heating tank (2-3 ton/hr is enought to keep 98°C).
I want to recover steam which is going to atm, and send it to heat chip washing system. Idea is to keep 3 barg, but adding new line to send rest steam to chip washing system, in order to reduce pressure valve opening close to zero.
I have two alternatives in new line:
- Put steam flow control (valve and flowmeter).
- Put steam pressure control (downstream to valve). For example 2 barg.
I dont know what is best solution in order to get good control.
Thanks in advance,
Anibal