Introduction
Steel containers are used for storing liquid or gas in a plant. This blog discusses the most common type of storage vessels,
plot plan arrangements, safety considerations, spill containment, pumping, and
general piping layout, Tank
Settlement for Piping Stress Analysis, Tank
Bulging effect or bulging effect of tank shells & stress analysis as per API
650 using CARSAR II.
Tanks
A
storage take is a container, usually for holding liquids, sometimes for
compressed gases (gas tank). Since most liquids can spill, evaporate, or seep
thorough even the smallest opening, special consideration must make for their
safety and secure handling. This usually involves building a boundary, or
containment dike, around the tank, so that any leakage may be safely contained.
Some storage tanks need a floating
roof in addition to or in lieu of the fixed roof and structure. This floating roof
rises and falls with the liquid level inside the tank, thereby decreasing the
vapor space above the liquid level. Floating roofs are considered a safety
requirement as well as a pollution prevention measure for many industries including
petroleum refining.
Type of Storage Tanks
There are various storage tanks used
for storage of raw material and for storage of final products etc. they are
mainly fix roof tanks, floating roof tanks, horizontal bullets and sphere and
the details are as follows.
A) Fix Roof Tank
Fix
roof tanks are used for liquids where tendency of evaporation is very less and
very high flash point. (E.g. fuel oil, water, bitumen etc.) The tank design
code is APL 650 and main part are bottom plate, shell and top roof which is
conical in shape and used steel section for supporting roof called rafters.
Nozzles data will be as per process requirement. Normally nozzles are inlet for
tank feeding, outlet which normally connected to pump, drain and vent which are
required at the time of maintenance, manholes for ease of maintenance, nozzles
level indicator and some spare nozzles. Cone roofs, dome roof and umbrella
roofs are usual. These are insulated to prevent the clogging of certain
materials, wherein the heat is provided by steam coils within the tanks. Cone
roof or fix roof tank is atmospheric tank used for very law pressure. Whereas Dome
roof tanks are meant for tanks having slightly higher storage pressure than
that of atmosphere (E.g. slop oil).
B) Floating Roof Tank
Floating
roof tank is used for high volatile fluids where evaporation rate is very high. Roof will float above liquid like
ship float above the water and the surface of the roof is touched above the
liquid surface which will minimize vaporization of the fluid. There is no any
special code for roof design, but shell design is as per API 650
Floating
roof tanks are broadly divided into external floating roof tanks (usually
called as floating roof tanks: FR tanks) and internal floating roof types (IFR
tanks).
IFR
tanks: IFR tanks are used for liquids with law flash-points (E.g. ATF, MS.
gasoline, ethanol). These tanks are nothing but cone roof tanks with a floating
roof inside which travels up and down along with the liquid level. This
floating roof traps the vapor from low flash-point fuels. Floating roofs are supported
with legs on which they rest.
FR
tanks: FR tanks do not have a fixed roof (it is open in the top) and has a
floating roof only. Medium flash point liquids such as naphtha, kerosene,
diesel, crude oil etc. are stored in these tanks.
C) Dome Roof Tank
Dome
roof tank is one type of fix roof tanks instead of conical roof, dome roof
(Dish type) roof is used which is stronger that conical roof and hence will
hold slightly higher pressure than conical roof tank and used for petroleum
industry for storage of very high amount of liquid.
D) Horizontal Tanks /Horizontal Bullet
Horizontal
tank design is as per ASME sec Vlll div.I. horizontal tanks installation is
very easy and can be installed above ground or if there is space problem then
can install underground also. There type of tanks minimizes evaporation loss.
Installation of instruments is very easy. Maintenance can be possible by giving
platform and ladder or staircase. Mounting of the tank is on saddle.to take
care of thermal expansion one saddle should be fix and another should be
sliding. foundation height can be decided as per the operating requirement and
piping requirement.
E) Spherical Tanks
As
flash-points of fuels go very law the tanks are usually spherical (known as
spheres), for storage of LPG, hydrogen, hexane, nitrogen, oxygen etc. Spherical
tanks are used for holding very high-pressure liquid or gases. Pressure holding
capacity is very high because of equal pressure distribution on surface.
construction cost of sphere is very high. Also weld points are more in
spherical tank which decreases efficiency of the equipment’s. There are some
reasons some countries /companies avoid using spherical tanks and horizontal
tanks are preferred instead of spherical tanks.
Other classification
which can be made for storage tanks are based upon their location in a
refinery:
1. COT- crude oil tankages
2. PIT-product and intermediate storage
tankages
3. Dispatch- dispatch area tankages
4. Utilities- tanks made in the power plant area,
for storage water etc.
5. OSBL
tanks- the first 3
types come under out side battery limit tankages
6. ISBL
tanks- these are
usually mini tanks which are found in the production units of a refinery (as
neutralization tanks,) water tanks e
Typical Arrangement of Tank Piping.
1.
Determination
of piping route
2.
Process
piping should not cross any other pipes if possible.
3.
Formation
of vent pockets
4.
Piping
from and to the tanks should run through the shortest routes.
5.
A
minimum distance of 500mm shall be secured between the dike and pipe support.
6.
Tank
block valves shall be provided with platforms which can also be used as a
walkway
7.
Valves
shall be arranged by aligning the flange surfaces
8.
Space
between two crossing pipes shall be at least 300 mm.
9. Valve accessories should be considered in determining spaces between closely arranged valves
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