virk
Chemical
- Oct 14, 2003
- 58
A customer of us describes the following problem:
In an ammonia (absorption) refrigeration installation one expansion valve group consists of shut-off valve DN25, control valve DN25, shut-off valve DN150 (expansion has taken place).
Between first shut-off valve and control valve a pressure gauge (manometer) is installed.
Normal "high" pressure of system is 12 bara. If this control valve is in normal working position the installed manometer shows approx. 10 bara. So we already have a pressure loss of 2 bars due to thin lines and long length.
Customer now says, if I completely open my control valve, net flow into the separator decreases, so I limited the valve to 80% opening.
At this moment after I thought about this problem some time, I am unsure whether customer perhaps misinterpreted something.
What do you think? Under which conditions this phenomenon can occurr, decreasing flow at higher valve opening?
Kind regards
In an ammonia (absorption) refrigeration installation one expansion valve group consists of shut-off valve DN25, control valve DN25, shut-off valve DN150 (expansion has taken place).
Between first shut-off valve and control valve a pressure gauge (manometer) is installed.
Normal "high" pressure of system is 12 bara. If this control valve is in normal working position the installed manometer shows approx. 10 bara. So we already have a pressure loss of 2 bars due to thin lines and long length.
Customer now says, if I completely open my control valve, net flow into the separator decreases, so I limited the valve to 80% opening.
At this moment after I thought about this problem some time, I am unsure whether customer perhaps misinterpreted something.
What do you think? Under which conditions this phenomenon can occurr, decreasing flow at higher valve opening?
Kind regards