1. Zeroth and First Law
of Thermodynamics
Introduction to Thermodynamics
2. Learning Outcomes
You will
State and explain the Zeroth Law of Thermodynamics
State the First Law of Thermodynamics and derive mathematical
relationship for a closed system
Derive relationships for Internal Energy Change and Enthalpy
Change in terms of specific heat capacitates of the substance and
temperature change
Derive relationship between specific heat capacities, and the
Universal gas constant for ideal gasses
Use First Law of thermodynamics together with ideal gas equation
to solve simple problems
3. Content
Zeroth Law of Thermodynamics
First Law of Thermodynamics
Derivations from First Law
Internal Energy and specific heat capacity under constant volume
Enthalpy and specific heat capacity under constant pressure
Relationship between specific heat capacities for ideal gasses
Examples
4. Zeroth Law of Thermodynamics
Let A, B and C (say is a thermometer) be three systems. If A and B are
separately in thermal equilibrium with C, then A and B are in thermal
equilibrium.
Thermal equilibrium: Two systems are in thermal equilibrium if they
could transfer heat between each other, but don't.
In Thermal
equilibrium
5. Zeroth Law of Thermodynamics
As a consequence of Zeroth law we can conclude that
“Temperature” a property that determines whether an
object is in thermal equilibrium with other objects
Two objects in thermal equilibrium with each other are at
the same temperature
If two objects have different temperatures, they are not in
thermal equilibrium with each other
6. First Law of Thermodynamics
First law of thermodynamics states that energy can neither
be created nor destroyed, it can only change the form.
For a closed system or a fixed mass:
Net energy
transferred to the
system as heat and
work
Net increase in
the total energy
of the system=
8. Example 1
A certain amount of air is compressed in a cylinder. The
change in internal energy of the air is 10kJ. Work required for
the compression is 500kJ. What is the amount of heat
transfer?
UWQ
Work done by the system - Positive
Heat supplied to the system - Positive
kJWUQ 45050010
Sign convention
Heat is rejected
Solution
9. Derivations from First Law
Consider constant pressure process
UWQ
HQ
pVUpVUQ
VVpUUQ
VpUUQ
)()(
)(
1122
1212
12
HTCQ p
Specific heats at constant volume and constant pressure
If Cp is Specific Heat Capacity of the substance;
TmcQ P
10. Derivations from First Law
Consider constant volume process
UWQ
Since there is no work transfer, UQ
If Cv is Specific Heat Capacity of the substance under constant volume ;
TmcQ v
Therefore; UTCQ v
11. Derivations from First Law
pVUH
mRTUH
TmRUH
TmRTCTC vp
mRCC vp
Rcc vp
v
p
c
c
= specific heat ratio
This is equal to 1.4 many adiabatic
process
Specific heat relations for ideal gases
12. Example 2
A 0.6kg copper piece at 100oC is dropped in to an insulated tank
containing 0.75kg of liquid water at 25oC.
Determine the temperature of the system when thermal
equilibrium is reached. Specific heats of copper and water
are:0.393kJ/kgK and 4.184kJ/kgK
For incompressible substances (solids and liquids) cp and cv
take same value
13. Take the copper piece and water as the system. The temperature
after equilibrium is reached is T2.
UWQ
U0
0 wcop UU
0)()( 1212 wwwcopcopcop TTcmTTcm
0)25)(184.4(75.0)100)(393.0(6.0 22 TT
CT o
24.302
Solution
14. Example 3
The temperature of 3.5kg of gas in a container is increased from
22oC to 39oC by heating it. The heat transferred during the process
is 25kJ. Calculate, treating the gas to be a perfect gas,
(a) change in internal energy and
(b) work done
The specific heats ratio and the molar mass of the gas are 1.4 and
28g respectively.
15. UWQ kJQ 25
12
1
TT
mR
TCU v
1
,1
1
mR
C
C
mR
C
mR
C
C
mRCC
v
v
vv
p
vp
)2239(
14.1
)028.0/314.8)(5.3(
1
)/(
12
TT
MRm
U o
kJU 17.44
17.4425 W
kJW 17.19 Minus means work has to be done on the system.
This implies that in order to increase the internal energy by 44.17kJ, 25kJ is not sufficient
Solution
16. Example 4
An insulated cylinder closed at both ends contains free moving
piston. One side of the cylinder is filled with nitrogen, and the other
side with air. Initial pressure and volume of each gas are 1bar and
0.01m3 respectively. The initial temperature is 20oC for both the
gasses.
The air in the cylinder is heated by means of an electrical heater
installed inside the cylinder until the volume occupied by the
nitrogen is reduced to 0.008m3
Find
(a) final temperature of air and
(b) Work done by air
(c) heat added to air
Cv for air is 0.718kJ/kgK and R for air is 0.287kJ/kgK. Adiabatic index for
nitrogen is 1.4
17. Applying ideal gas equation for air state 2 )1.......(222 aaaaa TRmVp
Applying ideal gas equation for air state 1 )2........(111 aaaaa TRmVp
From (1)/(2)
aa
aa
a
a
Vp
Vp
T
T
11
22
1
2
)3........(1
11
22
2 a
aa
aa
a T
Vp
Vp
T
3
111 01.0,29327320,1 mVKTbarp aaa
(a) Final temperature of air
Solution
18. Now find V2a NaNa VVVV 2211
008.001.001.0 2 aV
3
2 012.0 mV a
Now find P2a
Under equilibrium condition , P2a=P2N
NNNN VpVp 2211 Because nitrogen gas undergoes
adiabatic process for which
Polytropic index is 1.4
barbar
V
Vp
p
N
NN
N 367.1
008.0
01.0
)1(
4.1
2
11
2
19. KT a 6.480)293(
)01.0)(1(
)012.0)(367.1(
2
From equation (3) )3........(1
11
22
2 a
aa
aa
a T
Vp
Vp
T
(b) Work done by air
4.11
)01.0)(1()008.0)(367.1(
1
1122
NNNN
N
VpVp
W
kJWN 234.0
kJWa 234.0
20. kJkJWUQ 254.12234.002.16
UWQ
aava
aa
aa
aaav TTc
TR
Vp
TTmcU 12
1
11
12 )(
kJU 02.162936.480)718.0(
)293)(287.0(
)01.0)(10)(01.0( 5
Using first law
(C) Heat added to air
21. Example 5
In a piston cylinder device, 300g of saturated water vapor
maintained at 200kPa is heated by a resistance heater installed
within the cylinder for 10min by passing current of 0.35A from
220V source. The heat loss from the system during the heating
process is 2.2kJ.
Calculate (a) final temperature of the steam
(b) work done
22. )1.....(UWQ
kJVItQE 2.46)600)(35.0)(220(
kJQ 442.22.46
)2)....(( 12 hhmHQ
kgkJh /5.27061
From steam tables, at 200kPa and sat.
vapour. condition
(a) Final temperature
23. )5.2706(3.044),2( 2 hFrom
kgkJh /16.28532
From steam tables, when h2 = 2853.16 at 200kPa
CT o
47.1912
At 200kPa
T h
150 2768.8
T2 h2=2853.16
200 2870.5
8.27685.2870
8.276816.2853
150200
1502
T
24. )( 12 uumU
kgkJu /5.25291
From steam tables, at 200kPa and sat.
vapour. condition
U2 is the internal energy at 200kPa and at
191.47oC
At 200kPa
T u
150 2576.9
191.4
7
u2
200 2654.4
9.25764.2654
9.2576
150200
15047.191 2
u
kgkJu /2.26412
)5.25292.2641(3.0 U
kJU 51.33
From (1)
UWQ
kJW
W
49.10
51.3344
(b) Work done