dezirak
Chemical
- Oct 12, 2005
- 14
Currently modifying catalyst control system.
Current flow rates vary quite a bit by grade.
.5lbs/hr to 150lbs/hr liquid (0.88 S.G.) is the most striking flow range seen. I am estimating a controllability turndown required of about 300:1 to 500:1.
Current pump set up is a single stage diaphram pump, pulsation dampener, pressure regulator recycle after dampener, Coriolis meter after recycle, then flow control valve. In order to obtain these relatively large turndown ratios and bring the flow control valve OP into a controllable range, operations adjust the pressure regulator setpoint, pump micrometer (and subsequently the pulsation dampener), and tuning of regulator and control valve. This amount of adjustment results in a lot of inconsistency based on the knowledge and experience levels of the people on shift, which in turn may affect our quality due to flow variations. I should mention that the pressure varies downstream of our flow control valves from 60 psig to 140 psig depending on campaign. Maximum regulator pressure upstream of flow control valve is limited to 350 psig.
After speaking to pump vendor as to best course of action they recommended running the pump/recycle loop at a constant high pressure (300-350 psig) and flow while tackling the turndown issue at the control valve level. (An actuated micrometer is not an acceptable option due to limited turndown according to vendor).
Is it possible to get adequate control with a single valve? Is it possible to obtain this level of controllability turndown without resulting to 2 valves ran in split range?
Thanks
Current flow rates vary quite a bit by grade.
.5lbs/hr to 150lbs/hr liquid (0.88 S.G.) is the most striking flow range seen. I am estimating a controllability turndown required of about 300:1 to 500:1.
Current pump set up is a single stage diaphram pump, pulsation dampener, pressure regulator recycle after dampener, Coriolis meter after recycle, then flow control valve. In order to obtain these relatively large turndown ratios and bring the flow control valve OP into a controllable range, operations adjust the pressure regulator setpoint, pump micrometer (and subsequently the pulsation dampener), and tuning of regulator and control valve. This amount of adjustment results in a lot of inconsistency based on the knowledge and experience levels of the people on shift, which in turn may affect our quality due to flow variations. I should mention that the pressure varies downstream of our flow control valves from 60 psig to 140 psig depending on campaign. Maximum regulator pressure upstream of flow control valve is limited to 350 psig.
After speaking to pump vendor as to best course of action they recommended running the pump/recycle loop at a constant high pressure (300-350 psig) and flow while tackling the turndown issue at the control valve level. (An actuated micrometer is not an acceptable option due to limited turndown according to vendor).
Is it possible to get adequate control with a single valve? Is it possible to obtain this level of controllability turndown without resulting to 2 valves ran in split range?
Thanks