we are designing indirect water bath heaters to heat the well fluids from 40 Deg C to 55 deg C . The well fluids shall be heated in coils immersed in water bath. The water bath shall be heated by fuel gas. We would like to know if there is any recommended slenderness (Length /Diameter)ratio for...
Sir ,
I have to design the instrumentation for a heater treater having two different chambers for heating & treating the crude oil-water emulsion . The viscosity of incoming crude varies from 1-6000 Cp wheras final product shall be having viscosity of 900 Cp. Iam not sure at which values the...
sir ,
As desired by Monagas,the additional details for sizing of three phase separator are as follows:
Flow rate through three phase separator shall be 1000m3/day of liquid with water content varying from 20-40% and assiacoated gas of 75000m3/day .
The specific gravity of oil -0.84, gas -0.76 7...
sir,
I am working on three phase separator for oil & gas industruy . I am following API 12J but three phase separator is not covered in detail. Can you suggest some conventional method to aprroximately size a three phase separator.The retention time is assumed to be 5 Minutes for horizontal...
we are planning to construct a storage for soda-ash. we would like to know the type of flooring required for the same . If it is in the nature of tiles .
What is the type of tile?
What is the method of fixing the same ?
What are the appropriate standard ANSI/BS giving the laying of flooring...
we are planning to construct a storage for soda-ash. we would like to know the type of flooring required for the same . If it is in the nature of tiles .
What is the type of tile?
What is the method of fixing the same ?
What are the appropriate standard ANSI/BS giving the laying of flooring...
WE ARE HAVING ONLY ONE TRUNK LINE WHICH IS PRESENTLY USED TO TRANSPORT GAS . IS IT POSSIBLE TO SEND THE WELL FLUID( TWO PHASE ) ALONG WITH THE GAS AS WE WOULD LIKE TO SAVE ADDITIONAL LINE COST. WHAT ARE THE IMPLICATIONS? . IS SUCH A PRACTICE FOLLOWED ANYWHERE ELSE? THE EXISTING CASES MAY BE...
I WOULD LIKE TO KNOW IF IT IS POSSIBLE TO DO BATCH PUMPING OF NAPTHA AND CRUDE THROUGH THE SAME PIPELINE AS WE ARE PALNNING TO USE ONLY ONE PIPE LINE TO TRANSPORT THE TWO PRODUCTS IN DIFFERENT BATCHES.
FURTHER IS IT POSSIBLE TO USE THE SAME PUMP TO THE TWO PRODUCTS.
ANY SIMILIAR CASE MAY ALSO...
Thanks for the reply. It would be better if such an instance is qouted where submerged flare system has been designed and working satisfactorilly.
The problems in submerged flare line are plenty but the situation so demands that the flare line be submerged 1-2 meter below ground.
The reference...
Sir,
I would like to know if the flare line leading to flare can be buried 1-2 meter below the groung and top surface can be concertised . The flare knock out drum is planned to be kept near the installation and flare line approx. 90 m is planned to be taken underground.The flare tip would be...
Hello SAA,
Thanks for reference , it would be appreciated if you can refer any software, or any site available on net on this . The design book can also be referred to solve this problem .
regerds,
sssharma
We are having a vertical separator of dia 1424mm and height 4790mm . The heads are torispherical. The design pressure is 10 kg/cm2.This separator is planned to be used for separation of crude oil & gas at 6kg/cm2 (operating Pressure). The sp. gravity of crude is 0.8194 abd that of gas is...
