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kerosene storage tank

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BZLAM21

Petroleum
Aug 12, 2020
58
hi friends i want your help please

currently I am working on a new project and the design office suggested us tha the new kerosene intermediate storage tanks were will be fixed roof tanks with internal floating screen and nitrogen blanketing because floating head roof tanks will allow oxygen ingression and will be causing corrosion and fouling issues.

From a product contamination standpoint,
Is the fixed roof tanks the best solution to avoid corrosion and fouling issues caused by air contact with the feed?

what is the point of covering a tank with a fixed roof with nitrogen?

Thanks and best regards.
 
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Bouzitoune,

I'm not aware for kerosene that there is any issue with oxygen into the fluid.

In many countries, kerosene is stored in fixed roof tanks with open vents or for large quantities or warmer locations, external floating roof tanks.

You need to question the design office about the particulars of your case and get them to justify the additional cost.

The nitrogen blanket reduces emissions and prevents an explosive atmosphere being potentially present in the tank either above the internal roof or for a fixed roof tank.

"Kerosene" can cover many fluids. You also need to know the vapour pressure at your storage temperature before you can make any sensible decisions.

Remember - More details = better answers
Also: If you get a response it's polite to respond to it.
 
From my point of view, kerosene tanks are usually fixed roofs, with floating internal roofs. The nitrogen blanket is to prevent oxidation of kero, gum formation and also for safety reasons.

luis
 
in 30 years of refinery projects, I've seen kero stored in either fixed or floating tanks, but never blanketed with nitrogen.
by the way, OP is speaking of a "kero intermediate", without specifying its nature...
 
Dear All,

the kerosene flash point (ABEL CC IP170) is 55.5c°
density (D4052) is 792
volume to store is 8500m3
ambient temperature can reach 40c°

if the evaporation rate from the liquid surface will be reduced by the nitrogen blanket for what is used an internal floating roof? in that case it will be an additional cost!!!

Thanks in advance and best regards .
 
All depends on the size of your tank and pressure of the N2 blanket.

If it's v low / atmospheric, the N2 blanket may be overcome by the vapour which will start venting off.

Internal floating roof prevents much of the vapourisation.

What you really need to find is the graph or table of vapour pressure versus temperature. Flash point is about flamability, not boiling point or vapour losses.

If you're above about 11 psia then internal floating roof will be better / required to stop excessive vapourisation or you will need a pressurised tank at probably a few psi.

But "kerosene" means different things to different people. If this is general kero, then Ok, but aviation kerosene is a different beast and may require floating roofs.

Remember - More details = better answers
Also: If you get a response it's polite to respond to it.
 
tha data provided by OP would classify the "kerosene" as a low vapour-pressure liquid.
in fact the difference between flash point (55.5°C) and max storage temperature (40°C) is 15.5°C, well above the 15°F / 8°C required.
in this case, the vapour released from a vent would not create a flammable mixture and so a fixed-roof tank is safe.
of course, the client is free to ask more.
good luck!
 
Dear all,
1/ Please where can I find the table of vapor pressures as a function of temperature.
2/is the maximum temperature is equal to the ambient temperature? or it is fixed according to standards
Best regards
 
Am familiar with fixed roof tanks with N2 blanketing, but have never seen internal floating roof with N2 blanketing - simply irrelevant. Believe N2 blanketing is not required for straight run kero, but for kero derived from FCC or similar /delayed coker with significant quantities of olefins, have read that contact with O2 results in gum formation, and some acids with corrosion concerns. Internal floating roof type construction is typically used for more volatile products than 55degC FP kerosene where tank displacement vapor emissions are HSE concerns.
 
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