Oxygen Bomb Calorime ter A00201079 [Type text] [Type text] [Type text]
A00201079 OXYGEN BOMB CALORIMETER 21/11/2013
THE OXYGEN BOMBCALORIMETER
Objectives To understand calorific values of combustible fuels To determine the calorific value of combustible fuels
Apparatus An oxygen bomb calorimeter Crucible Thongs Steel wire Combustible fuel samples Oxygen supply Balance Benzoic acid Steel bucket
Figure 1 the oxygen bomb calorimeter (Parrinstrument company)
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Figure 2: Oxygen bomb crucible (Parr instrumentcompany)
Introduction Combustion in essence is the chemical combination of a
combustible fuel with oxygen and this in turn results in the
production of heat energy. Combustion is achieved by combining
the two key elements of combustion a fuel and oxygen, at an
elevated temperature or an ignition temperature. The chemical
breakdown is simple enough with a decent understanding of the
periodic table. The air around us supplies the oxygen, which
will bond with hydrogen, carbon and other smaller elements
within a fuel to produce the by product of heat. The principle
of combustion is vital to modern day industry and engineering.
Equipment and technology is required to burn solid liquid and
gaseous fuels to a high heat recovery standard and to ensure
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the desired amount of heat is obtained from any fuel and
ensure very little waste product is left over after combustion
of the fuel. The basic functionality required from such
equipment designs is namely to provide a supply of oxygen and
mixed fuel in the desired ratio. Too much of either of these
ingredients would lead to improper and unsatisfactory
combustion of the fuel itself. The high temperature during
combustion must also be confined and retained (access
engineering).
Wood coal and simple fuels like this are the combustible
substances which in coming in contact with an air supply
produce large amounts of heat energy. The term combustion
itself refers to the exothermal oxidation of a fuel by oxygen
within the air at a rapid rate to produce a high temperature.
This is usually with a spark ignition and the appearance of a
flame. Most fuels contain carbon or carbon and hydrogen,
combustion involves the oxidation of carbon to carbon dioxide
and also hydrogen to water any sulphur which is present is
oxidised to sulphur dioxide while any mineral matter within
the fuel forms the waste product as. Coal is a complex fuel
and will undergo thermal decomposition during the stages of
combustion which then gives simpler products which are in turn
oxidised to give carbon dioxide and water.
Fuels are classified in two separate classes
1. Primary fuels – naturally occurring fuels. Fossil fuels
such as coal, oil and gas
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2. Secondary fuels – these are fuels derived from the
primary fuels due to treatment processes examples of
which would be gasoline, petroleum etc
A good fuel should have a high calorific value and in doing so
should produce large quantities of heat energy when combusted.
When a fuel contains hydrogen there are two distinguishable
calorific values the gross and the net values. The gross
calorific value refers to heat which is obtained when the
water which is a product of the combustion is then condensed
as a liquid. The net value refers to the water vapours which
are not condensed and escape along with the hot gases. This is
the lower value. It is the value of the produced heat when the
unit mass of the fuel is burned completely and the products of
combustion are allowed to escape.
a simple calculation of net calorific value can be shown in
this form
Hydrogen in a fuel reacts with oxygen to give water
H 2 + ½ O2 gives H2O
2H = ½ O2=H2O
Atomic weights then are taken for each element
2parts H=16partsO2=18partsH2O
1parts=8 parts=9 parts
So for every 1kg of hydrogen 8 kg of O2 is required for the
ideal combustion
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The calorific value of a fuel is described and defined as the
quantity of heat required which is produced by the complete
combustion (the online dictionary)of a specified mass of a
particular fuel. This quantity is generally expressed in
joules per kilogram (the online dictionary). The gross or the
higher value is heat which is available from a fuel when
complete burning has taken place , it is defined as the total
heat liberated by the complete combustion of the fuel
(department of energy and climate change). This particular
value is determined by measuring the heat removed when cooling
the products of combustion to a standard reference temperature
(department of energy and climate change). Calculations then
determine the lower value which is also referred to as the net
value. This then equals the gross calorific value minus the
latent heat of the water vapour or wet products formed from
the combustion of hydrogen and also from any moisture which
may be present in the combusted fuel (department of energy and
climate change). This net value is more representative of heat
available when a fuel is used as a heat source in industry or
home use and when the fuel is burned in boilers and furnaces.
The specific latent heat of water vapour is usually
unrecoverable from the exhaust gases. The use of gross net
calorific value tends to differ from industry to industry.
Engine and gas turbine makers will use net calorific value
where as boiler manufacturers would use the gross value when
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labelling how efficient their piece of plant is. The fuel
itself is bought on the grounds of its gross value and in turn
its energy consumption on site or in plant operation is
expressed in terms of the gross calorific value of the fuel
(department of energy and climate change).
The oxygen bomb calorimeter experiment is a very important
test in determining the specific calorific value of a
designated volume of a fuel. Its primary function is to assess
the gross calorific value which is the gross heat of
combustion of a material. The bomb calorimeter is able to
determine the potential maximum heat released by a fuel while
undergoing complete combustion (GBH International).
A test sample of fuel of a known mass is combusted under the
standard conditions the volume remains constant within the
pure oxygen atmosphere which is housed in a calibrated bomb
calorimeter. The calorific value found under these set
parameters and conditions is calculated via the observed
temperature rise in the calorimeter vessel itself while also
taking account for heat losses. The calorimeter vessel itself
is submerged in an outer water bath the heat of the water in
the water bath is constantly monitored. An embedded computer
control mechanism a keypad and an LCD enable monitoring and
usage of the test while in operation.
Procedure
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The tank fill located at the rear of the calorimeter must
be full with deionised water
The water mains must be switched on
The oxygen supply must then be switched on. The pressure
gauge on the regulator furthest from the cylinder should
read 450 PSI
The power button on the calorimeter is then switched on.
Wait 3 minutes for the system to start up
Main menu will be displayed on the touch screen
Calorimeter operation is then selected which leads to a
sub menu
The operating mode can then be selected. the operation
mode will be standardisation for initial set up and
calibration of machine and then determination for all
experiments
Then the heater are pump are turned on via the main menu
20 minutes approximately will elapse before the
calorimeter will warm up sufficiently to 30 degrees
Celsius. once it reaches this desired temperature it is
allowed to stand for another ten minutes
The test procedure is now ready to begin with the desired
set up in place
The bomb chamber is now opened via means of undoing the
screw cap on the top
2 millilitres of water is poured into the chamber
The o rings on the bomb chamber are lubricated with water
The fuse wire must then be cut and is usually a nickel
material. The wire is cut to 100mm length and the ends of
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the wire are placed through the two designated holes in
the sample holder. The adjoining clips are then pushed
down to ensure it is held in place. the exact weight of
the wire is accounted for internally in the machine
Figure 3 the wire The chamber is then placed on the spring balance and the
value is zeroed
The benzoic acid sample is then place within the chamber
and its weight of .9465 grams is accounted for and
recorded
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Figure 4 benzoic acid The chamber with the benzoic acid sample is then placed
within the chamber holder and it is ensured that the
nickel fuse wire sits just above the sample and does not
contact the sample in any way
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Figure 5 the chamber and sample The inlet valve is then opened on the chamber seal
The bomb holder seal is pushed down into the chamber and
screwed onto the male thread until sufficiently tight
Figure 6 screw down cap The valve on the chamber seal is then closed
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The oxygen pipe is then connected to the coupling on the
bomb inlet valve
Figure 7 oxygen connection The o2 fill command is then pressed on the screen and 60
seconds are allowed to pass . when this time has elapsed
the machine will automatically stop the fill
The oxygen pipe coupling is then removed
An empty bucket appropriate and designated for the test
is then placed on the spring balance for weigh in and the
weight recorded
This is approximately 790 grams
The weight is accounted for and the weight of the bucket
zeroed
2 litres of de ionised water must then be poured into the
empty bucket until the reading is exactly 2000 grams
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The bucket is then placed in position in the calorimeter
chamber within the machine the handle must be placed down
towards the back
The bomb chamber is then lifted via the provided tongs
and placed in the bucket of water
The bomb sits vertically in the bucket
The bomb tongs are then removed from the locating holes
and any residual water on the tongs is shaken off back
into the bucket to ensure no upset in mass of water
The two ignition wires are then connected to the bomb
chamber into the terminal sockets located on the top of
the chamber. When attached they must be left in such a
way that they will not become entangled in the stirrer
attached to the lid of the calorimeter chamber. the
connection of the wires to each port does not matter as
regards arrangement of the connections
Figure 8 the stirrer13
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Now close down chamber door
The calorimeter process can now begin. the operating mode
is standardization when calibrating at the beginning
using the benzoic acid sample but the determination
method is used for the other tests
The bomb I.D number is 1,2,3,4 etc
Sample I.D number is 1,2,3,4 etc
The start button is pressed and the sample weight .9465
grams is entered
The calorimeter now takes over the procedure and conduct
the test. During the test period the calorimeter computer
will display PREPERIOD on the screen and will then also
display an alarm just before the bomb is fired within the
calorimeter. Once the bomb has fired the status bar on
the computer will read POSTPERIOD
The red line on the graph is the bucket temperature and
the black line is the jacket temperature
This is a temperature versus time plot as every 12
seconds the computer reads the temperature
The printer built into the calorimeter will then produce
automatically the results once the test is completed
When the operation is complete the chamber is opened and
the two connectors are disconnected
The bucket and bomb are lifted out simultaneously
Bomb holder removed from the bucket
The inlet valve is undone slightly and vents any gas left
within the bomb holder
The seal cap on top is screwed off
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The bomb seal and the chamber holder are then pulled out
The interior area of the bomb holder is examined for any
remains of the fuel like soot or ash. If such evidence
exists the test result is not true and must be discarded
The bomb holder is cleaned out
Turn off the oxygen at the tank
Turn of water at mains
Turn the heater and pump off via the computer screen
Turn off mains supply to calorimeter
The above explained procedure is the means for testing
all specimens.
Figure 9 entire apparatus
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Above is an example of result one we believe it is for coal
but due to time constraints in the lab we were unable to
obtain our own results due to malfunctions within the
calorimeter set up. The calorimeter miss fired for each test
and we were unable to obtain any of our own results
0 100 200 300 400 500 60025.11525.12
25.12525.13
25.13525.14
25.145
f(x) = 1.94765635327555E-05 x + 25.1270556691661
f(x) = NaN x + NaNBenzoic Acid Calorimetry Data
Post-ignition Line
Time (s)
Temp
erat
ure
(C)
Figure 11 shown here is a typical example of atemperature versus time combustion of benzoicacid within the calorimeter obtained from
online (1312)Species Benzoic acid NaphthalenePellet mass (±0.0001 g) 1.03 0.4880Wire mass initial (±0.0001 g)
0.0160 0.0163
Wire mass final (±0.0001 g) 0.0034 0.0073Δmfuse wire (g) 0.0126 ±
0.000140.0090 ± 0.00014
Wire heat of combustion (cal/g)
1400 1400
Benzoic acid heat of combustion (MJ/kg)
26.454 ---
(1312)
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Above shows an online result for benzoic acid along with
naphthalene the calorific value or heat of combustion of the
benzoic acid is 26 Mj/Kg
The formula with which data from this experiment can be
applied to is
Hc= WT-e1 –e2 –e3/M
Hc= gross heat of combustion or
calorific value
T = Observed temperature
W (EE) =energy equivalent of the
calorimeter in use or the amount of
energy require to raise temp of
calorimeter by one degree
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E1 =heat produced by burning nitrogen
portion of the air in the bomb to
form nitric acid
E2 =the heat produced by the
formation of sulphuric acid from the
reaction of sulphur dioxide water and
oxygen
E3= heat produced by the heating wire
and cotton thread
M = overall mass of sample
ConclusionIt is disappointing that we as a group were unable to obtain
our own results. The calorimeter miss fired each time and due
to this we ran out of time to obtain a satisfactory result for
ourselves. We did obtain as seen above a previous result from
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a previous class session and were able to distinguish what
each reading formed on the data sheet corresponded to. The
bomb calorimeter procedure itself in essence is a simple but
perhaps time consuming procedure and is the simplest way to
obtain the calorific value of a given mass of a substance. To
draw a conclusion on results we did not obtain is rather
difficult for any experiment. But one objective can be deemed
a success from the experiment and corresponding lectures in
that my personal understanding of the importance of knowing
the calorific values of certain fuels is of great importance
in the engineering world. Fossil fuels still power the vast
majority of automation and electricity production for industry
and knowing the correct fuel to air ratio is of vital
importance in the modern day world of carbon emissions. It is
essential to know the exact amount of fuel so as not to have
too much waste or un combusted product at the end. It in turn
is also to have the correct amount of oxygen so as to burn off
the fuel sufficiently. Insufficient oxygen for the mass of
fuel also leads to leftover fuel and the full calorific value
of the fuel is not obtained. In industry these ratios become
very important as cost saving and cost effectiveness are at
the heart of any business and when you are purchasing vast
quantities of oil coal or gas you need them to be cost
effective in their operation. The right fuel also is a very
important factor when applied to industry and heat generation.
They bomb calorimeters ability to determine the exact
calorific value of a fuel is of great benefit to the consumer
as the greater the calorific value the greater the heat
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produced during combustion. So when applied to industry the
correct fuel can be chosen for different procedures. For
example a cement kiln would need a temperature of about 1500
degrees Celsius minimum where as the simple boiler at home
would not need temperatures near this level to create the heat
required. So instantly the calorific value of the fuels used
for each operation would come into play. A fuel with a very
high calorific value would be good for the cement kiln as it
would provide the massive heat required for its operation
where as the simple home boiler would be sustained with a fuel
of much lower calorific value and a slow burn.
Having completed the experimental procedure i fully understand
how to use the oxygen bomb calorimeter and this is of great
benefit because if asked to repeat such an experiment i would
feel very confident in doing so and as a budding engineer this
would be of vital importance for many tasks in the future
Bibliography(n.d.). Retrieved 12 2, 2013, from www.personal.psu.edu/users/c/p/cpf5020/.../457%20finalreport3.docx
access engineering. (n.d.). Retrieved 12 2, 2013, from http://accessengineeringlibrary.com/browse/steam-plant-operation-ninth-edition/c9780071667968ch06
department of energy and climate change. (n.d.). Retrieved 12 2, 2013,from http://chp.decc.gov.uk/cms/fuel-calorific-value/
GBH International. (n.d.). Retrieved 12 2, 2013, from http://www.gbhinternational.com/specsbomb.htm
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