6. Any action which can change the state of the
system
Types
Reversible
o Slow
o Can be reverted at any point by small operation
force
Irreversible
o Fast
o Can’t be reverted
7. Intrinsic / Intensive- does not depend on
the amount of system.
Extrinsic / extensive- depended on the
amount of system
PVT P,T,V/2 P,T,V/2
8. Heat –
Heat added to the system (+)
Heat release by the system(-)
Work-
Work done on the system (+)
Work done by the system (-)
10. change in energy is depends on effect of
heat (Q) and effect of work(W).
E=Q+W
No work , no heat exchange then
change in system energy
E=0
11. 1. When small change in ex. Pressure is=Pex
2. Then small change in volume =dV
3. And work
dW= -Pex.dV ( –ve bcz of opposing force)
12.
13. The max. work which a system can do
w/o any external energy take.
Can’t be calculated
But change in energy can be calculated
(?>>,?<<)
14. FUNCTIONS
State F.-
It doesn’t matter which
way choose to reach
from E1 to E2
ex- internal energy
Path F-
Depends up on path
ex- work,heat
E1,P,V,T
E2,P’,V’,T’
15. Energy is conserved.
Energy can’t be created , can’t be
destroy ,it can only be converted one
form to another form.
For isolated system - E=0
For open and closed system-
E =Q+W
16. Change in internal energy at constant
pressure=
E=Qp-P. V
Change at constant volume=
E=Qv-P*0
E=Qv
So heat given at constant volume is equal to direct
change in internal energy
17.
18. enthalpy
It is a thermodynamic state function
Like internal energy it can’t be exactly
calculated
H=E+PV
H= E+P. V (at constant pressure)
H=Qp-P. V+P. V ( bcz E=Qp-P V at
constant pressure)
H=Qp so heat given at constant
pressure =direct change in enthalpy
19. Molar/specific heat capacity
Amount of heat in joules required to rise 1 mole
of a substance 1 Kelvin.
at constant pressure If we have n mole gas, increased
it temp T and heat expended Qp
Then Cp= Qp/n. T
Similarly to constant volume = Cv=Qv/n. T
(when a system absorbs heat, the temp increases the heat
capacity of a system is defined as the ratio of change in heat to
the change in temp).
we have to prove that Cp-Cv=R……1
Qp/n. T-Qv/n. T= Qp-Qv/n. T = Cp-Cv
we know that H=Qp (enthalpy), and E=Qv (internal energy).
20. H- E/n. T = Cp-Cv…………2
But we know H= E- P V,put in eqn 2
P v/n. T=Cp-Cv……………...3
We know PV=nRT
P( V) = nR( T) ( we are working at cons. pressure )
P V/n. T= R (put the value in eqn 3)
So Cp-Cv=R where R is 2 cal/mol/k
21. Kelvin statement- In a cyclic process
,heat can not be 100% converted to
work.
Clausiu’s statement- Heat does not
spontaneously flow from cold to hot.
23. S=Qreversible/T
Entropy =0 (at truly reversible process) &
>0 for an irreersible
Gas in
container
Reversible process at Q
heat
Constant temp
24. Ideal cycle
Initial state = final state
No human involved
4 steps – 2 isothermal (T cons) ,2 adiabatic ( no heat
exchange)
1st step (thermal expension)
P
v
a
b
Power step
26. Why not compress the gas is isothermally and bring it back
to initial position?
If we do that work net =0
Why adiabatic expansion?
we want to perform less work during compression to make
cycle viable .
One of the way is to do that is to reduce pressure i.e.- reduce
temp.
In first two step system did the work.. After 2 step we will
perform.
a
b
27. Step 3-isothermal compression
Compression will increase heat so its use
reservoir.
Constant heat is to reduce pressure. Because
low pressure =less work .
T2
28. Volume is close to initial but temp. is low..
Step 4- gas is compressed to bring it back to
originally state.
29. Introductory chemistry for the environmental science (second
edition)
by R.M. HARISON
Chemistry of Atmosphere
by P.S. SINDHU
https://chem.libretexts.org
www.edu.thermodynamics
www.study.com
www.brightubengineering.com
Web.mit.edu