×
INTELLIGENT WORK FORUMS
FOR ENGINEERING PROFESSIONALS

Log In

Come Join Us!

Are you an
Engineering professional?
Join Eng-Tips Forums!
  • Talk With Other Members
  • Be Notified Of Responses
    To Your Posts
  • Keyword Search
  • One-Click Access To Your
    Favorite Forums
  • Automated Signatures
    On Your Posts
  • Best Of All, It's Free!
  • Students Click Here

*Eng-Tips's functionality depends on members receiving e-mail. By joining you are opting in to receive e-mail.

Posting Guidelines

Promoting, selling, recruiting, coursework and thesis posting is forbidden.

Students Click Here

Jobs

Oil Recovery

Oil Recovery

Oil Recovery

(OP)
Iam working on an FPSO Vessel.Presently producing from only one wellof 6000barrels/day.The stabilisation Separator was initially operating at design temperature of 80degrees centigrade and the flare was slighly on with smoke(loss of hydrocabon).On reduction of temperature to 62 degrees,production increased to 6200barrels.It is now noticed that the Sorage tank relief valve  vents more frequently.Considering the gain in Production,could somebody advise on other ways of avoiding a catastrophe (if any) or finetuning of the plant for optimisation while reataining my present production.

Red Flag This Post

Please let us know here why this post is inappropriate. Reasons such as off-topic, duplicates, flames, illegal, vulgar, or students posting their homework.

Red Flag Submitted

Thank you for helping keep Eng-Tips Forums free from inappropriate posts.
The Eng-Tips staff will check this out and take appropriate action.

Reply To This Thread

Posting in the Eng-Tips forums is a member-only feature.

Click Here to join Eng-Tips and talk with other members!


Resources