CLX Independent PID

Andybr, if you look at the Advanced Conrol thread you can see all I needed is one ( initial and final ) set of data from a step response. I can the change the closed loop time constant to make the response faster or slower using the initial set of data. Plus I can simulate the response quickly like Gerry did. On processes that are dangerous or take a long time, similations likes Gerry's are the way to go since they can be done off line.

The ZN methods we developed before we all had PCs with lots of processing power. The ZN methods are not statistically sound because one is using just a few subjective points to determine the gain.

Parting shot. I think it is a crime that the people who build the plants don't provide a good estimate of what the gains should be. If they truely engineered the system they should know. As a customer I wouldn't accept the system without a model. If the engineers don't have a model then they really don't know how their system works.
 

Similar Topics

Controller: 1756-L84E v.35 Prosoft MVI56E-MNETC for ModbusTCP/IP I'm having an issue with some of my write commands. The write command that...
Replies
0
Views
206
I have several Avery scale units and they are configured as Generic Ethernet modules, and I am actually reading the data fine for the weight...
Replies
2
Views
436
What's the best way to move a tag value from the panelview+7 to the clx plc. We display amps from a power meter on the panelview screen, read in...
Replies
1
Views
404
I'm running into an issue migrating a PLC-5 using the newer Logix Designer Export when opening a saved .ACD from RSLogix-5. It has multiple RIO...
Replies
2
Views
630
We have two sites that are stranded with no line of site, they are handled by phone/modem with a chain that includes: Stranded site (client)...
Replies
5
Views
918
Back
Top Bottom