I solved similar problems by adding a PIC to control the upper limit of the
FIC. 

Recently, I have been wondering if it would not be more efficient to link
the output of the PIC to the BIAS input of the FIC.  (The output of the PIC
would have a range of -100 low to 0 high.)  But what I have done works, so I
am reluctant to change anything.  The only advantage that I see to this new
scheme would be that the upper limit would still be available for operator
(or engineer) use, if needed.

Chuck Jones
Refinery Automation Technologist
A.E. Staley Mfg. Co. -- Lafayette South Plant
765.477.5324 - Office  | 765.420.4431- Pager


-----Original Message-----
From: Lance Dusing [mailto:[EMAIL PROTECTED]]
Sent: Friday, July 06, 2001 9:12 AM
To: Foxboro DCS Mail List
Subject: Process Control


Hi everyone,

Here is a process control question I have been pondering.

Under normal process conditions, the control looks like this...

        |--|
        |FT|--
        |--|  |
              |
|--|    |---|  ->|---|    |---|
|LT|--->|LIC|--->|FIC|--->|VSD|
|--|    |---|    |---|    |---|

However, if the pressure in the line with the VSD gets to large, corrective
action needs be taken.
How is the best way to control this?
Limit the FIC hi output limit with logic? 
Switch to a PIC?
Anything else?

Lance


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