Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I...

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Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

Transcript of Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I...

Page 1: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

Development of EoS for Vapours & Gases

P M V SubbaraoProfessor

Mechanical Engineering Department

I I T Delhi

Models for Highly Bountiful Phase…..…..

Page 2: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

Behaviour of Vapour

= interatomic potential, Joules.• r = separation of molecules, nm (mean Free path).• r = equivalent “hard sphere” radius of molecule (overlap of

electron clouds).• At high T, high p, collisions in the repulsive part of – positive

deviations from constancy.• At low T, moderate p, collisions in the attractive portion of –

negative deviations from constancy.

Page 3: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

P – v- T Relation

• Greatest need for EoS of saturated and superheated steam.

Tv

aRTpv

•R and a are constants.

•The is called as Rankine’s Equation of state, 1849.

n

T

Tcc

0

0

• The specific volume of A vapour:

v = f (p,T)

dTT

fdp

p

fdv

pT

bT

Tc

p

RTv

n

0

0

Page 4: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

P – v- T Relation

• Callender’s Characteristic Equation for saturated and superheated vapours.

bcp

RTv

•R and b are constants.

•c is a function of temperature and it is called as co-aggregation volume.

n

T

Tcc

0

0

• The specific volume of A vapour:

v = f (p,T)

dTT

fdp

p

fdv

pT

bT

Tc

p

RTv

n

0

0

Page 5: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

Pressure Volume Diagram

bT

Tc

p

RTv

n

0

0

Page 6: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

Van der Waals EOS

• One of the oldest but most extensively used of the EOS of non ideal gases

• Any EOS model must reproduce graphs such as that of the previous

RTbvv

ap

2

•a, b are the Van der Waals constants for the particular gas;

•for water: a = 0.5658 J-m3/mole2; b = 3.049x10-5 m3/mole,

abavvRTpbpv 23

p

RTvideal

Page 7: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

JO H A N N E S D . V A N D E R W A A L SThe equation of state for gases and liquids

Nobel Lecture, December 12, 1910

I intend to discuss in sequence:

(1) the broad outlines of my equation of state and how I arrived at it;

(2) what my attitude was and still is to that equation;

(3) how in the last four years I have sought to account for the discrepancies which remained between the experimental results and this equation;

(4) how I have also sought to explain the behaviour of binary and ternary mixtures by means of the equation of state.

Page 8: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

Van der Waals EOS

RTbvv

ap

2

•a, b are the Van der Waals constants for the particular gas;

•for water: a = 0.5658 J-m3/mole2; b = 3.049x10-5 m3/mole,

Page 9: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

Van der Waals CoefficientsGas a (Pa m3) B (m3/mol)

Helium 3.46 x 10-3 23.71 x 10-6

Neon 2.12 x 10-2 17.10 x 10-6

Hydrogen 2.45 x 10-2 26.61 x 10-6

Carbon dioxide 3.96 x 10-1 42.69 x 10-6

Water vapor 5.47 x 10-1 30.52 x 10-6

abavvRTpbpv 23 RTpvideal

Page 10: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

Van der Waals Isotherms

Page 11: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

Isotherms of Real Gases

Page 12: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

Improved Cubic Equations of State

Page 13: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

The constants a, b, c, Ao, Bo varies with substance

Page 14: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..
Page 15: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

Compressibility Factor

• The deviation from ideal gas behaviour can also be expressed by compressibility factor, Z.

• The ratio of volume of real gas, Vreal to the ideal volume of that gas, Vperfect calculated by ideal gas equation is known as compressibility factor.

RT

pvZ real

p

RTvideal

ideal

real

v

vZ

Page 16: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

• Compact description of non-ideality: the compressibility factor,

• Z 1 as p 0 (ideality)

• Z < 1 at low T, moderate p (point A)

• Z > 1 at high p, high T (point B)

Page 17: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

Generalized Compressibility Chart

Reduced Pressure pR = p/pc

Reduced Temperature TR = T/Tc

Page 18: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

VdW EOS & Compressibility

• a represents the attractive part of the potential; with b = 0, the VdW EOS gives a smaller v for the same T than the ideal gas

• b represents the repulsive portion of the potential; with a = 0, the VdW EOS gives a larger v for the same T than the ideal gas

• The VdW EOS is easily expressed in the forms p(T,v) or T(p,v).

• For the v(T,p) form, or, equivalently, Z(p,T):

vRT

a

vbRT

pvZ real

1

1

Page 19: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

The ideal gas equation of state may be written several ways.

Page 20: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..
Page 21: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

What More Happens at System Boundary during Change of State

The Happenings Which are our Benefits!!!

Page 22: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

Global Wind Patterns : The Simple Resource

Page 23: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

The Ancient Green Method for Better Living

Traditional Egyptian architecture in Ancient Egypt as demonstrated on the Pharonic house of Neb- Ammun, Egypt,

19th Dynasty, c.1300 BC.

Persian: بادگیر bâdgir: bâd "wind" + gir "catcher“

Arabic: ملقف malqaf

Eastern Arabia:بارجيل barjeel

Page 24: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

An ancient Idea for Better LivingWindcatcher (Bagdir)

Page 25: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

Evolution of Wind Turbines

• Wind is a clean, safe, renewable form of energy.• Although the use of wind power in sailing vessels appeared in

antiquity, the widespread use of wind power for grinding grain and pumping water was delayed until – the 7th century in Persia, – the 12th century in England, and – the 15th century in Holland.

• 17th century, Leibniz proposed using windmills and waterwheels together to pump water from mines in the Harz Mountains.

• Dutch settlers brought Dutch mills to America in the 18th century. • This led to the development of a multiblade wind turbine that was

used to pump water for livestock.• Wind turbines were used in Denmark in 1890 to generate electric

power. • Early in the 20th century American farms began to use wind

turbines to drive electricity generators for charging storage batteries.

Page 26: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

The Modern Green Idea for Better Living : Wind Power

Page 27: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

What happens When there is a change in state?

• Any of these happenings is/are useful for engineering world?

• Does it consume any resource?

• How to recognize these Happenings?

• Thermal In-equilibrium

• Mechanical In-equilibrium

• Chemical In-equilibrium

• Any combinations of above.

• These are happenings or actions or path functions or interactions.

• Present only during a change of state.

• What action is work transfer?

• What action is Heat transfer?

• What action is Mass transfer?

• How to differentiate?

Page 28: Development of EoS for Vapours & Gases P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Models for Highly Bountiful Phase…..…..

Mechanical Work Tranfer• Work is a mechanical concept given by the expression:

• F is a force and s is a displacement

• Work is a scalar product

• Force components along the displacement vector only can do work

• Force components perpendicular to the displacement vector cannot do work.

• This relationship will be useful to find work required to raise a weight, to stretch a wire or to move a charged particle through a magnetic field.

sdFW

.

2

1

21 . sdFW