thread798-156994
in OLGA software , in the TRENDDATA, PROFILEDATA output variables I can found many slug flow characteristics like slug length (LSLEXP) ,bubble length (LSBEXP), slug frequency but i can found slug volume , So how I can calculate the max liquid slug volume and average...
After conducting a FERA (Fire and Explosion Risk Assessment) and QRA (Quantitative Risk Assessment) study, what is the the recommended risk level / radiation contour to placement / install of fire hydrants. and can we install fire hydrants within the 10^-4 (or 0.0001) risk level contour (ALARP...
is this correct According to NFPA 30, the recommended minimum separation distances between crude oil tanks are as follows:
For non-fire-resistance-rated tank construction:
For tanks with a capacity of more than 15,000 gallons (56,780 liters), the separation distance should be a minimum of 1.5...
The open and close drain system design is based on segregated system (The Open Non-Hazardous Drainage System is segregated from all other open or closed drain systems.), What is the API code which cover this point
is there a minimum inventory for the standalone tank to install the Lightning protection system, ex. if we have stand-alone storage tanks with 1000 bbl crude oil, should we install a Lightning protection system?
if I have a standalone crude oil storage tank in the desert with a capacity of 200 M3 , is it necessary to install a fixed fire fighting system or I can depend on portable fire fighting
in a storage tank farm, a bund wall is existent around each storage tank and the distance between tanks is big and enough that mak the radiation from any tank pool fire to the nearest tank is less than 10 kw/m2 , and the storage tank capacity around 10000 BBl crude oil,
Is it mandatory to...
I hope if one can guide me to a spreadsheet /website /software which can help in estimating greenhouse gas emissions from the flare system depending on the quantity and composition of flared gas.
I search for Compact high-pressure centrifugal pump to handle flow rate in the range of 5000 BPD & discharge pressure in the range of 3000 PSI with suction pressure 50 PSI but the restriction point will be the area as this pump will be installed in offshore oil and gas platform with only 3M*3M...
in inner diameter sizing for piping of production manifold for multiphase well , are we use the same correlations and procedure as we sizing flowline or there is special requirement for this case , also is the flow regime and flow assurance study need to be consider when sizing wellhead...
what procedure i must follow for sizing sizing pressure & vacuum relief valve (PVRV) for atmospheric crude oil storage tank . and what the best software for handle this task
What the factors consider when sizing control valve for oil and water separator outlet , as an example in my process plant , separator oil outlet is 10 inch and installed control valve is 6 inch while the water outlet 8 inch and installed control valve is 6 inch . is the above related to...
what the best book cover the design of produced water treatment system (water produced from formation in oil and gas industry), and is there any software help in that.
in design of two phase and three phase separator , what the factors must be consider while outlet Nozzles sizing for the separator , when i size using some excel spreadsheet the nozzle can't easily handle the liquid level in the separator and when increase this size it handle out this liquid...
i work in oil and gas company , the produced water TDS about 240,000 PPM we want to decease it to 40,000 PPM so we can safely disposal it to the sea , what is the best process or Technic we can use for reducing TDS to the accepted limit. i search the forum and found the following closed thread...
What is the best Produced Water Treatment Packages & Systems Suppliers ?, i search for good Suppliers for oily water treatment Packages or facilities for treated water before disposal it to reduce oily water content , BOD ,COD & TDS
