| What You Need to Know to Have a Tank Calibrated |
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Many people who are in the position of having to have a tank
calibrated have little knowledge of what is involved in the calibration.
Some may not even know why the tank needs calibrating at all.
To help you assess your requirements we have prepared this general
outline of tank calibration.
Why do tanks need calibration at all? [top]
If you do not need to know what is in, or what has gone out of, a
tank and if spillage or overfilling is of no concern, then you probably
do not need to have a tank calibrated. If you require any indication of
quantity then you need a calibration of some sort.
At its simplest, a calibration of any vessel involves a knowledge of
the dimensions of the vessel and a calculation of the total volume.
For a water tank this may be enough and you may not even need to call
in a specialist.
At the other end of the scale, a tank can be measured precisely and
calculations can be made to take into account factors such as
hydrostatic expansion of the tank during filling and thermal expansion
of the tank shell in service.
For most situations in Australia where you are selling from a tank
or where customs duties are levied on tank contents, you will need to
have a tank calibrated by an organisation certified to do so by The
National Organisation of Testing Authorities or by your local State
Government Trade Measurement Department.
For the purposes of this exercise we shall assume that you have
decided that you do require a precise calibration of your tank.
What are the options in calibrating a tank? [top]
For any tank, whether it is a stationary tank or on a road, rail or
marine tanker, there are two broad options. It can either be calibrated
volumetrically, i.e. by measuring in volumes of liquid, or by physical
measurement and calculation of the volume. In some cases it is clear
which method is appropriate and in others either method can be used.
Generally, volumetric methods are suited to small tanks or tanks
that are irregular in form where mathematical models cannot be
applied. Volumetric methods include both metering volumes into or out
of the vessel to be calibrated and addition of volumes of water from a
certified prover.
Road tankers are generally always calibrated by volumetric methods,
rail-cars can be done either way, whilst large vertical tanks are
normally calibrated by physical measurement.
Food products, brewery and wine vats can be done either way or
sometimes by a combination of the methods.
We will consider volumetric and physical methods of calibration
separately.
Calibration of Tanks for Petroleum and Petroleum Products to ISO, IP
and API Standards.
The above organisations have a range of Standards to cover the
calibration of vertical, horizontal and spherical fixed storage tanks
as well as rail tankers and barge tanks.
The available Standards are as follows: ISO 7507 - 1 Vertical Tanks
Strapping method ISO 7507 - 2 Vertical Tanks Optical Reference Line
Method ISO 7507 - 3 Vertical Tanks Optical Triangulation Method
IP 202 Part II Section 1 Vertical Tanks Measurement Method IP 202
Part II Section 2 Horizontal & Inclined Tanks Measurement Method
IP 202 Part II Section 3 Liquid Calibration Method IP 202 Part II
Section 4 Spheres & Spheroids Measurement & Volumetric IP 202
Part II Section 5 Ship & Barge Tanks IP 202 Part II Section 6 Road
& Rail Vehicles
API 2550 Upright Cylindrical Tanks Measurement Method API 2551
Horizontal Tanks Measurement Method API 2552 Spheres & Spheroids
Measurement Method API 2553 Barges Measurement Method API 2554 Tank
Cars Measurement Method API 2555 Liquid Calibration of Tanks
Vertical Tanks: [top]
Although there are differences in the application of some of the
above Standards, there is a lot of duplication. Even where there are
differences in the measurement or calibration methods, the difference to
the end user is often less than any measurement errors involved, either
in the calibration or the measurement of the product.
In Australia, being a nominally metric country, it makes sense to
use the ISO Standard for upright cylindrical tanks. ISO 7505 is almost
a re-write of IP 202 Part II Section 1. The only real difference is
the calculation that involves temperature correction during tank
calibration. The ISO and IP Methods score over the API method in that,
for various reasons, they are more directly applicable to computerised
calculation.
There are two methods in common use for the physical (measurement)
calibration of the shell of vertical tanks.
The original method is by strapping. Strapping is the process of
measuring a tank by physically measuring the tank strakes with a
calibrated steel tape at several levels on each course of plating.
Strapping is a good method for small tanks that have scaffolding.
The other method often employed in Australia is the Optical
Reference Line Method. This method involves strapping the tank just
once at an accessible level, called the reference level. In this
method, an "optical plummet", a device used to establish a
true perpendicular, is used to measure the radial offset at several
levels on each course of plate. This procedure is repeated at
approximately four metre intervals around the tank and the
circumference at each level is calculated from the sum of the
differences between the reference level and the measured level.
The optical reference line method has a lot of advantages over
strapping. It also has a couple of disadvantages.
The advantages of the optical method are:
1. Optical Measurement is
safer than strapping. There is no need to access the outside of the
tank, which is normally done in a bosuns chair. The optical plummet
operator sits at the base of the tank whilst an assistant manoeuvres a
magnetic scale trolley on the tank shell from behind the hand rail on
top of the tank.
2. Optical calibration is faster than strapping in most cases, with
less impact on other operations in the area. A typical 20 metre
diameter tank could have the shell measured in only a few hours.
3. There is a better traceability of the field data from the
calibration. The data from which the tank is calibrated is recorded
for later calculation and verification, as are calibration records of
the optical plummet. With strapping there is the problem of the tape
sagging during measurement and the real difficulty of repeatable
measurements whilst the operator is suspended off the side of the
tank, trying to maintain 50 Newtons of tension on the strapping tape.
4. As a side benefit of the optical method, the data from which the
circumferences are calculated will also yield information on the shape
of the tank shell. It is a simple matter to process the data to
determine the verticality of the tank shell and to determine the "roundness"
of the tank. This is essential information to the engineer who wants
to fit floating blankets or roofs to vertical tanks. It is also
information that can be useful in determination of any settlement or
subsidence of the tank in service.
5. It is simple to optically calibrate a lagged tank. After
measuring tank diameters internally, the plummet can be used inside
the shell.
6. It is probably possible to calibrate a tank in stronger wind
conditions than is safe for strapping. (This may depend on how brave
the tank strapper is!)
7. There are some disadvantages of the optical method: 1. The equipment
used is more expensive than that required for strapping. Optical
plummets cost thousands of $'s and are delicate instruments. Even with
optical equipment, it is still necessary to use strapping tapes for
the reference measurement.
8. It is difficult to use the optical plummet in wet weather, as
rain on the lenses makes vision difficult.
9. The existence of scaffolding can prevent the effective use of the
magnetic scale used for optical measurements. Strapping is often
indicated in this case.
10. Calculation of the tank volume tables is more complex, although
with computerised calculation routines, this is no longer a problem.
Calibration of tank bottom volumes: [top]
There are two methods that can be used to calibrate the volume below
the dip-plate in a vertical tank:
1. The tank floor profile can be surveyed physically, using an
engineers level or theodolite, and the volume calculated
mathematically.
2. The tank floor can be calibrated volumetrically, using a meter or
volumetric prover and water.
As before, each method has advantages and disadvantages:
The advantages of the physical survey are: [top]
1. Physical survey is faster, cleaner and does not require the
availability (and following calibration, the removal) of large
quantities of water. A typical physical survey on a 20 metre diameter
tank may take only a couple of hours. To fill a 20 metre tank with a
bottom volume of 30 m3 may take two or three hours to fill and most of
the day to empty and clean. A tank of 35 metres diameter and a bottom
volume of 100 m3 may take five to six hours to fill and a day to empty
and clean. Physical survey would still take only a couple of hours.
2. During a physical survey it is simple to measure the precise
relative height of all tank internal structures. These heights can be
related to the dip-plate to give the tank operators accurate figures
for when tank structures are covered with product.
3. The data obtained during the physical survey can be processed to
give the tank owners data on floor profile, tank tilt and settlement.
This can be invaluable for comparison with previous or subsequent data
to determine tank shell settlement and stresses.
4. Physical survey data from the bottom survey can be related to
external measurements during tank hydrostatic testing to determine
ground loading response.
5. Physical survey is less intrusive than metered water methods. The
tank is immediately available for use after the calibration and unlike
the volumetric method, does not require any cleaning after removal of
water.
The advantages of volumetric calibration of
tank bottoms are: [top]
1. For extremely irregular tank bottoms, or for tanks with extreme
tilts, a volumetric calibration can sometimes be more accurate. The
accuracy of a physical survey can be improved by use of more measurement
points, but if extreme accuracy is required, a volumetric calibration
may be the best option.
2. If the tank is not safe to enter, it is sometimes possible to
calibrate volumetrically if the dip-plate is visible from the manhole,
or even if it is not, by dipping the tank whilst filling.
It is sometimes thought that a volumetric calibration is more
accurate that a physical survey because of tank floor sponginess or
spring. Our experience and information that we have from Europe, is
that a water column of 2 metres is required to eliminate 90% of tank
floor spring. In reality, it is not practical to fill any but the
smallest of tanks to this level and floor spring is not a major
problem in small tanks.
We have performed some practical research on a number of 30 meter
diameter tanks, calibrating by both meter and physical survey. We have
found the results to be within 1% in all the tanks concerned, which
amounted to less than 1000 litres.
We have found that it is difficult to determine levels in a tank to
within 3 mm during a water bottom calculation, due to meniscus/
surface tension effects on the dip-plate and to splashing due to the
operator being in the tank to observe the filling process. The
previously mentioned 100 litres equates to 1.4 mm in a 30 metre
diameter tank.
In some circumstances it can be unsafe to work in a tank during
water bottom calibration, due to gases from contaminated water. In
these circumstances it is not possible to obtain relative height
measurements from the water surface to tank structures.
Calculations of tank capacities for vertical
tanks: [top]
Tank capacity tables are calculated from tank circumferences. The
following factors are taken into consideration during calculation:
1. Tape rises during strapping (i.e. welds or laps, manhole doublers
and other obstructions.)
2. Shell temperature and tape calibration
temperature during strapping.
3. Physical characteristics of the tank
shell material (Young's modulus, thermal expansion factors etc.)
4.
Difference in temperature between calibration and working conditions.
5. Paint and plate thickness, inside and outside the tank.
6. Tank
expansion during calibration (if the tank is not empty).
7. Tank
expansion from liquid head pressure in service/ density of product
stored.
8. Tank tilt.
9. Effects of positive and negative deadwood on
tank volumes.
What conditions are required for a vertical
tank calibration? [top]
Most vertical tanks can be calibrated in one working day if done by a
physical measurement. There are some other considerations:
1. If the tank is new, it should have a full hydrostatic test prior
to the calibration.
2. The tank shell coating should be cured, as a soft coating may be
damaged by the strapping tape or the wheels of the magnetic trolley.
(Some trolleys have narrow alloy wheels that will even damage a cured
coating. Our trolleys have soft plastic wheels to minimize the
problem).
3. Ideally there should be no other work being performed on the
tank, as welding, grinding, hammering and sandblasting all make the
shell vibrate, which makes optical measurements difficult. However, we
all exist in the real world and if the time window is tight (and it
always is) we can usually work with or around other operators.
4. The tank should be clean and gas free for entry. Most terminals
have their own requirements for confined space entry and issue their
own work permits. We have our own atmospheric monitoring equipment and
we have training in gas free inspection. We will issue our own permits
if there is no satisfactory system in operation. If the tank is not
clean for entry, there are alternative options for bottom calibration
as previously mentioned.
When should a vertical tank be re-calibrated? [top]
A tank may change its calibration whenever the operating conditions
are changed. This could be for a variety of reasons. For example:
1. Change of product density - this will effect the expansion
characteristics of the tank, hence the volume.
2. Change of operating temperature - most tanks are calibrated for a
shell temperature of 15 degrees. A large change of operating
temperature will alter the tank increment (i.e. its ltrs/ mm.)
3. Any modifications to the tank or the dip plate - i.e. new pipe
inverts, fitting a stilling well, floor repairs, floating roof
modifications, changes in deadwood, etc.
4. Settlement of the tank with resultant changes in the tank
geometry.
It is generally recommended that a tank should be re-calibrated at
not more than 10 year intervals, especially considering tank
settlement. In areas where tank settlement or ground subsidence is
known to be a problem, an external settlement survey can be performed
without tank entry, to marked positions on the external protrusion of
the annular plate. These heights can be referenced to a datum level in
the terminal and also to the internal tank calibration data.
The calibration of horizontal tanks: [top]
Horizontal tanks can be calibrated to either the API or the IP
Standards. There is little difference in the end result. The calculation
routines for both Standards have been around for a long time and neither
one takes advantage of the ability of computers to perform laborious
calculations. The API Standard in particular, makes extensive use of
tables for various corrections, rather than providing formulae. We use a
method that follows the IP method, but exceeds the precision of the
method in that we can process greater degrees of tank tilt and greater
ranges of head shape with much better accuracy. The Standards make
several assumptions on the volumes of tank heads, where we are able to
calculate volumes precisely.
Horizontal tanks can be calibrated either volumetrically or by
physical measurement.
What is involved in the volumetric
calibration of tanks: [top]
Most commonly, volumetric calibration is performed by adding liquid,
usually water, to a vessel in small volumes. The liquid can either be
metered in through a calibrated "Master Meter" or dropped from
a calibrated volumetric prover. After the addition of each new volume,
the level is measured and recorded. Any corrections required for
temperature or meter factor may be applied to the levels and a table or
dipstick is manufactured for the tank.
No corrections are applied for tank expansion, as this occurs during
the filling process. There is a potential problem here for pressurised
tanks or tanks holding products having densities different to the
measuring liquid. If the tank service conditions for pressure, either
hydrostatic or otherwise, are different from the calibrating
conditions, there will be a volume error.
The problem of similar conditions for calibration and use also
applies to tanks that may be installed on different angles from which
they were calibrated. If the tank inclination is different from the
calibrated condition, there may be errors in the volume.
Volumetric calibration is ideal for tanks which require dipsticks,
as there is no need to apply other corrections, and a dipstick can be
made directly from the recorded levels.
The process does require a volume of water equal to the tanks
capacity to be available during calibration and requires that the
vessel be clean enough to allow the water to be disposed of after
calibration.
It can also be quite a time consuming process for a large tank and
it may interfere with other work that is being done in the area.
What is involved in the physical calibration
of horizontal tanks: [top]
Horizontal tanks are generally manufactured in a workshop and
transported to site. With physical measurement methods tanks can be
calibrated either in the workshop or after installation, as long as the
tank if installed on the designed inclination.
Horizontal tanks can be calibrated by either internal or external
measurement.
External measurement is suited to tanks that are situated above
ground, with clear access to the tank shell heads. Tanks do not need
to be empty or clean for external calibration, although it is not
generally possible to measure tank deadwood on tanks that are in
service. The tank dimensions are determined by a series of
circumferences taken along the tank barrel and by measuring the
profile of the heads. We determine the head profile by erecting a
reference plane across the end of the tank and measuring a series of
points across the head. A problem with external measurements on tanks
in service is that it is difficult to establish the height of the
dip-plate/ striker plate. This is not an insurmountable problem, but
it is the source of calibration errors on horizontal tanks.
Internal measurement is our preferred method, as it enables more
precise measurements to be taken and less assumptions made on the tank
construction. A series of internal diameters are measured with an
internal tank gauge (a device similar to a large internal micrometer),
barrel lengths are measured and the head profile measured with a
purpose built head measuring gauge.
Deadwood can be measured precisely, as can the heights of the
dip-plate etc. Obviously for internal measurement, the tank must be
clean and gas free for entry.
For either internal or external measurement, the reference height
must be measured and if the tank is pressurised, special measurements
for tank gauging systems, slip tubes etc., must be taken.
Calculation of tank capacities for horizontal
tanks: [top]
Tank capacity tables are calculated from tank diameters, barrel
length and head profile data. The following factors are taken into
consideration during calculation.
1. Tape rises during strapping (i.e. welds or laps and other
obstructions.)
2. Shell temperature and tape calibration temperature
during strapping.
3. Difference in temperature between calibration and
working conditions.
4. Paint and plate thickness, inside and out of
tank.
5. Tank expansion during calibration (if tank is not empty).
6.
Tank expansion from pressure in service.
7. Tank tilt - this is
critical in horizontal tank calibration.
8. Location of dip tube
position with regard to barrel.
9. Effects of positive and negative
deadwood on tank volumes.
Notes: [top]
1. There are no "average values" for millimetres of product
on tank tables for horizontal tanks. Obviously the ltrs/mm value changes
for every level in the tank.
2. In the case of pressurised tanks, tables
can be issued for different working pressures or factors can be given
for pressures different from the usual working pressure.
What you should look for in a tank
calibrator: [top]
Whilst the mathematics of tank calibration are relatively
straightforward, to have a thorough understanding of all the principals
and factors involved requires some study.
We believe that the person who measures your tank requires a
thorough knowledge of the Standards, the measurement procedures and
the calculations involved to ensure that the correct measurements are
taken.
NATA is the organisation responsible in Australia for regulating the
Standards of metrology laboratories. Any tank calibration company
accredited to NATA is audited annually to ensure that their quality
system and equipment is maintained to the required standards and that
the companies personnel are competent to perform the work.
What tends to happen in Australia is that a company may hold NATA
registration in one location and use any staff available in another
location to perform field measurements. This does not automatically
mean that the work performed is shoddy or inferior, but it does mean
that there is less control over the training of staff, the calibration
of equipment and the accuracy of data.
The calibration company that you choose should also be able to
demonstrate a knowledge of safe practices in your terminal. In
particular, they should be trained in confined space entry procedures
and should have the necessary equipment to work safely in confined
spaces and at heights.
The calibration company should be able to offer prompt service. To
calculate an average tanks calibration table may take eight hours, but
there is no reason why you should not be able to request a faxed
calibration table within 24 hours of the field operator leaving your
terminal. You should also be able to expect to receive the finished
table within a week.
Obviously, we hope that you will come to us. We believe strongly
that tank calibration is an important part of terminal stock control
and we treat it accordingly.
Liquid Measure Australia is a division
of a global network, Intertek Testing Services - Caleb Brett.
Liquid Measure Australia , is committed to providing all aspects of
tank calibration. We will not send out inexperienced or unqualified
operators to measure tanks.
If you choose to use Liquid Measure Australia for your tank
calibration, the field operator that you see calibrating your tanks in
your terminal will be able to discuss all aspects of the calculation
of your tables and answer all your questions.
LMA "A True Measure Of Quality
Calibration - Making Every Drop Count!"
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