PetarKnezevich
Chemical
- Apr 25, 2012
- 4
Hi,
I'm a chemical process engineer working in oil & gas. I often have to review operating envelopes and I sometimes have difficulty conveying information to operators regarding complex systems.
Could I get your comments and suggestions on good ways get information across?
I have attached a simple chart that I once produced for control room team when I had to put a restriction on the entry pressure into a gas pipeline based on the arrival pressure at a downstream station (PSVs were chattering because the operating pressure was too close to the set pressure).
The graph is a simple (to me) way to find the desired pipeline inlet pressure to maintain the downstream station pressure below 86 barg depending on the pipeline flow rate. It is based on the actual pressure, temperature and flow data from the data historian.
Regards,
Petar
P.S. We changed to pilot operated PSVs and that solved the chattering problem.
I'm a chemical process engineer working in oil & gas. I often have to review operating envelopes and I sometimes have difficulty conveying information to operators regarding complex systems.
Could I get your comments and suggestions on good ways get information across?
I have attached a simple chart that I once produced for control room team when I had to put a restriction on the entry pressure into a gas pipeline based on the arrival pressure at a downstream station (PSVs were chattering because the operating pressure was too close to the set pressure).
The graph is a simple (to me) way to find the desired pipeline inlet pressure to maintain the downstream station pressure below 86 barg depending on the pipeline flow rate. It is based on the actual pressure, temperature and flow data from the data historian.
Regards,
Petar
P.S. We changed to pilot operated PSVs and that solved the chattering problem.