If you look attached sketch along with picture then you will note that there is two production manifolds each with 20" dia. one manifold is located about 2 km away from 2nd one. Joining in one point and then routed to production separator which 100 meter away. we don't have record of this...
Hi,
We found baffle plates in production line before joining another production line. Production separator is 100 meter away from the tee joint. a sketch and photo of baffle plates are attached. can anyone please explain the purpose of these baffles plates. theory / concept of these baffles will...
Sir, I always got more confidence after reading your answers and posts as many experienced engineers, even not foresee the cost of failures.
Many thanks
George,
Even he is chasing red herring, then how to move forward with the selection of Multiphase pump. May be you have gone through multiphase pumps selection as well.
That I know whilst I need the basis of concept selection. GVF is the basic information for pump selection whilst actual GVF is unpredictable due to well behaviors and consequently pump will fail particularly when wells are produced with ESP pumps. I need more information on this side.
Hi All
I'm searching multiphase pump selection / sizing guidelines as there is no specific information available. can anyone support with selection criteria or guidelines for multiphase pumps for oi & gas fields.
Thanks
Pipeline profile attached.
Any how, problem solved after increasing pipeline diameter, 4" to 6"
For Flow assurance, compositional tracking, PVT file routine failed while, PVT feed file work, can you let me know why this happening.
Thanks...
Hi all,
I'm continuously facing problem for multiphase flowline simulation, Olga simulation giving warning for multiflash failure and fluid update for flow path. File generated with black oil method, well test data GOR=2664, oil 55% and water 45%.
WARNING Compositional Tracking PVT routine for...
RVP Properties
The RVP properties can be calculated using the following correlations:
Reid VP at 37.8 C
True VP at 37.8 C
API 5B1.1
API 5B1.2
ASTM D323-73/79
ASTM D323-82
ASTM D4953-91
ASTM D5191-91
ASTM D6377-16
Aspen API
Modified ASTM
Note: Since ASTM D6378-10 is very similar to ASTM D6377-16...
Hi George,
Hysys measure RVP and TVP at 100 F, even pressure and temperature conditions are different. further, TVP calculation includes water and nitrogen while my stream has only hydrocarbons. I'm confused on TVP, why Hysys considered water plus nitrogen and oxygen as well.
Hi All,
I noted in my simulation, Bubble point, RVP and TVP are very much different from each other, especially RVP and TVP, can someone explain this difference as both measured at 100F and pressure 450 psig.
Thanks
no need to worry, this installed some 40 year ago and flowmeter just few months back, before, tanker was loading and dipstick was used to measure the quantity, now they want to measure with flow meter, just waste of money.
Flow meter design parameters.
Design flow:200, 500, 700 m3/hr
Design pressure: 16.6 barg
Operating range: 13,40,50 m3/hr
Operating pressure: 5 barg.
I think problem with meter settings, our guys set max flow 50 m3/hr.
This is for your information and comments if any.
Best regards
Pierreick,
Methanol is single phase liquid. but will ask instrument guy for signal connection. vendor specialist was not present the moment they commissioned.
