Two setpoints to control a pump

sameer

Member
Join Date
Jan 2003
Location
Texas, USA
Posts
7
I have a VFD driven pump that needs two setpoints. One is level setpoint at which the pump will start and stop. And second is pressure setpoint as we want to maintain a particular discharge pressure in the system (50 psi). So as long as the level is above the setpoint the pump will run but will ramp up or down to maintain a discharge pressure of 50 psi.
can this be done?
 
I have a VFD driven pump that needs two setpoints. One is level setpoint at which the pump will start and stop. And second is pressure setpoint as we want to maintain a particular discharge pressure in the system (50 psi). So as long as the level is above the setpoint the pump will run but will ramp up or down to maintain a discharge pressure of 50 psi.
can this be done?

Sure.
What is the application?
Which PLC are you using?

Must the pump run all the time?
 
The level control potion shoulf function like a start/stop circuit with a latch coil. The pressure control can be obtained with a PID. What controller are you using?
 
The most common approach is to use the analog pressure to start the pump and ramp it up and down in speed to maintain constant pressure using a feedback loop, PID or other. Float switches are provided in the wet well of the pump as a low level alarm that will stop the pump to prevent damage and annunciate the abnormal condition to the staff. A second high level float switch is provided above the normal operating range to annunciate an alarm.
 
i would bet sameer wasn't planning to include a plc ???

Few drives offer the option of a pid control and you may use something like a cheap 4-20mA relay to give start and stop but at the end...you will spend more in engeeneering around limitations than using a small plc
 
i would bet sameer wasn't planning to include a plc ???

Few drives offer the option of a pid control and you may use something like a cheap 4-20mA relay to give start and stop but at the end...you will spend more in engeeneering around limitations than using a small plc

I guess at that point we can only wait until the VFD info is given. Sorta strange, why post on a PLC forum if you dont plan on using one..:unsure::confused:o_O

Edit: Not implying that he wasn't planning to use a plc, just it would be strange if he wasn't
 
Last edited:
Just curious, what PLC are you using?

I would use a scheme where when the level drops too low the PID is placed in program manual mode and the output set to zero. When the level rises to the start level you return to auto mode.


Another option is to use a common control scheme called a low select, where you have two PIDs, one controlling level and one controlling pressure. Which ever PID has the lowest output is selected and the other non-selected PIDs integral sum is synchronized with the selected PIDs output. This is easy to do with a PLC/5 or a Control-Logix, and can be done with a SLC/Micrologix with some careful hoop jumping. A low select will keep your pump running as your approach minimum but slow it down instead of completely turning it off. You will have to determine if that is suitable for your process.
 
I guess at that point we can only wait until the VFD info is given. Sorta strange, why post on a PLC forum if you dont plan on using one..:unsure::confused:o_O

Edit: Not implying that he wasn't planning to use a plc, just it would be strange if he wasn't

I'm looking to see but at some point in my world, customers are always looking for low cost way of doing things. You are right it is a plc forum but some peoples here can answer other related questions about industrial controls like VFD controls and sometimes we request them for it :)
And to my opinion, this case would became a challenge without a plc
 
Yes you could use a level transmitter in you sump to start the pump on high level and stop the pump at low level (or alternatively low and high level switches). Use a PI controller to control discharge pressure via your VFD. Is it possible that you could have a scenario where more liquid is entering your sump at a higher rate than that which can be pumped out resulting in your sump level rising too high? If so how would you want to close off the supply to the sump?
 
I have some toshiba g9s that will do this. Maybe its my freshness in the industry but I can't really see any sizable company only wanting to control the drive locally but have other operations in or around the area.
 

Similar Topics

Hi guys, I'm working on controlling two pumps with a single PID loop. I've been doing searches in the forum and with Google so I have the...
Replies
12
Views
7,093
Hello all, If I have a closed loop system/pid loop to control steam and have different setpoints to control the same loop. How should I go about...
Replies
6
Views
2,444
I am working on a project using AB PLCs and PanelView HMIs. There is a desire to allow control loop setpoints to be provided through the HMI or...
Replies
11
Views
3,685
HI everyone. I have a Micrologix 1400 paired with a PV Plus 7. What is the "best" or "correct" way to change setpoints and have them retained...
Replies
4
Views
2,458
Hi, We have modbus tcp implemented in s7-1200. For now it has been only control and status. Now we want to change settings. I have never done it...
Replies
14
Views
4,321
Back
Top Bottom