Hi to everybody.
I need some halp ....
I have stream in pipeline consist of vol% 45% gas, 54,98% oil (emulsion of water in oil)and 0,02% sand.
I would like to ask, does anybody know cyclon which separate at same time sand from gas and oil fluid.
Cyclone - for gas fluid
Hydrociclon - for liquid...
Hello
We have gas well for the 89% of methan.
Our well is 860m deep
The temperature on the bottom is 60 celsiouse
WE MUST TO CALCULATE HOW MUSCH IS THE TEMPERATURE ON THE WELL HEAD?
HOW CAN WE CALCULATE THE TEMPERATURE FALLING?
THANKS TO EVERYBODY IN ADVANCE!
MARKO
I have dehidration colume for natural gas.
I need to choose the best type of the zeolit for removing the water!
1.) What is the princip for choosing? Where i can found the difference between zeolits for the choosing?
2.) How can i calculate how much of that zeolit do i need for my removal of...
I NEED TO FIND THE BEST SOLUTION FOR THE COALESCER ELEMENT IN MY OIL WASTEWATER SEPARATOR!
WHAT ARE THE CRITERIES WHICH I NEED TO FOLOW TO FIND THE BEST SOLUTION FOR COALESCES ELEMENTS IN MY SEPARATOR?
DO YOU HAVE SOME LINK OR WHATEVER?
THANKS IN ADVANCE TO EVERYBODY!
MARKO
Hi everybody!
I need help about corrosion again
I have CO2 flow with 6000kg/h where water in tube is crawling 16.5L/h on the bottom ....
I need to choose the best way to protect tube of corrosion. The corrosion rate is right now 0.34 mm/year.
My design life of tube must be 20 year!
Well i...
I look how to convert molar % to volume %!
I have gas mixture at pressure 80bar/1160psia and temperature 47 C (calsiouse)/320,15K
IT IS CONSTIST OF:
methane 8.99% molar
ethane 1.21% molar
propane 1.04% molar
butane 0.60% molar
penthane 0.23% molar
hexan 0.16% molar
heptan 0.06% molar
octan...
i HAVE A CO2 STREAM IN PIPELINE!
HOWEVER I HAVE SOME 3000ppm of H2O inside of the stream!
iN MY CONDITIONS I MUST USE INSIDE INHIBITOR!
I would like to know how to calculate VOLUME OF THE INHIBITOR (wichever) WHICH I NEED TO USE AS A REZISTENT TO CORROSION!
THANK YOU EVERYBODY 100 OF TIMES!
Dearest people i have problem probably quite easy but i can not find any information about that!Well:
i have:
-1000m carbon steel gas pipeline,
-at the inlet temperature is 47 celsious,
-the preasure is 73 bar,
-the pipeline is below graund,
-temperature of ground is 4 celsiouse,
I NEED...
Please is there somebody who can help me about
What kind of additions do we use for corrosion in pipes in which flow CO2 high preassure!
THANKS THANKS THANKS !
Hello to everybody!
I would like to ask for what ever kind of help about this theme!
I have task to DESIGN SIDE MIXER in the within tank for the diesel oil.The mixer must be axial propelere.
I WAS SEARCHING ABOUT THIS THEME EVERYWHER AND I DID NOT FOUND MOSTLY ANYTHING,only and just for the...
