Ok I am going to try a cheat a little and see if those on the list have worked with tough pH control problems and may have some ideas that would speed up my response to a problem here on site. We have a pH controller that seemed to be working over the years that now the process engineers have learned to hate. We used a PIDA. The liquid volume changes frequently going into the vessel and we use a lime feeder to correct the pH. That feeder has at times presented it own opportunities, however in the past when it was working correctly operations seemed to be happy. Any ideas on perhaps a different control block or scheme would be helpful. Thanks Robert Balmer Senior Application Analyst/Programmer CCST Climax Molybdenum Co. 2598 Highway 61 Fort Madison IA 52627 (319) 463-2206 Please consider the enviroment before printing this and all emails _______________________________________________________________________ This mailing list is neither sponsored nor endorsed by Invensys Process Systems (formerly The Foxboro Company). Use the info you obtain here at your own risks. Read http://www.thecassandraproject.org/disclaimer.html foxboro mailing list: //www.freelists.org/list/foxboro to subscribe: mailto:foxboro-request@xxxxxxxxxxxxx?subject=join to unsubscribe: mailto:foxboro-request@xxxxxxxxxxxxx?subject=leave