Steam Power Generation Pascal Tobaly IUT de St Denis Département Génie Industriel et Maintenance (G.I.M.) Welcome students of the international course on Power Generation Groeningen The netherlands November 19th 2003
Outline A bit of history Basics First law: Internal Energy Second Law: Entropy Heat Engine: Thermodynamic cycle Fluid flow: Enthalpy Liquid vapor Equilibrium: Water and Steam Power plants A schematic Steam Power Plant Simple Rankine cycle Power calculations Superheating ReSuperheating Back pressure turbine Regenerative cycle
A BIT OF HISTORY Hero of Alexandria: First century b.c.
A BIT OF HISTORY (Continued) Hero of Alexandria: First century b.c.
A BIT OF HISTORY (Continued) Denis PAPIN (1647- 1712)
A BIT OF HISTORY (Continued) Newcommen (1712)
A BIT OF HISTORY (Continued) Watt (1769)
First Law of Thermodynamics Energy is a constant If the internal energy (U) of a system increases, then it may have been increased by addition of heat ➔ Work ➔
from the outer world
U 2−U 1=W Q
Second law of Thermodynamics Entropy (S) of an isolated system increases It will eventually increase until equilibrium is reached If entropy decreases in a given system then entropy of the outer world must have been increased by a greater amount. This may be possible only because there are energy exchanges between the system and the outer world
Q ∫ T ≤S 2−S 1 e The equality stands for a reversible transformation
Fluid Flow and Enthalpy Fluid flowing through a machine 2 2
2 1
V V h 2−h1 − =wuq 2 2 = specific enthalpy = Velocity = Usable work per unit mass of fluid q = Heat per unit mass of fluid
1
h V wu
machine
In terms of Power: 2 2
2 1
V V ˙ Q˙ mh ˙ 2−h1 − =W 2 2
W˙
Q˙
= mechanical power = heating power
2
HEAT ENGINE THERMODYNAMIC CYCLE High temperature Heat reservoir
Th
Efficiency
W =∣ ∣ Qh
Carnot:
Tc ≤1− Th
Qh (Heat input) engine Work W Qc (heat loss) Tc
Low temperature Heat reservoir
Liquid - vapour equilibrium Manometer Thermostat Gas
Vapour pressure curve
Pressure Critical point
solid liquid
Supercritical fluid vapor Tc
Temperature
Dryness fraction mg x= mg ml
Definition: P
(m = mass) Properties
L
M
v−v l x= v g −vl
G
h−h l x= h g −h l v
vl
v
vg
v = specific volume h = specific enthalpy
Entropic Diagram Water
-
Enthalpy
-
Steam
P=
cte
Mollier Diagram
Saturated vapor T=Cte
P
=
cte
et
T
=
cte
Entropy
Data on the internet
NIST Webbook http://webbook.nist.gov/chemistry/ Many physical properties including saturation properties as a function of Temperature and superheated vapor properties. Page of this department http://www-gim.iut-stdenis.univparis13.fr/thermo/thermo.html
Steam Turbine
Steam Turbine Rotor
Rankine cycle (Wet) B
Turbine
T
A A
B
Shaft
Boiler E
D
E Pump
C
D
C
S Condenser
Energy and power calculations Turbine H
B
A
Energy
V 2C V 2B h C −h B − =wu q 2 2
Power
W˙ =m˙ wu =mh ˙ C −h B
C
Boiler
E
S
D
Mollier Diagram
2 B
2 E
V V − =wuq Energy h B −h E 2 2 Power
˙ m˙ q= mh Q= ˙ B−h D
Isentropic efficiency
Is not an efficiency ratio of real work to ideal (isentropic) one (with same final pressure) H 0 - 1 isentropic 0 - 2 real
0
1
2 S
Mollier diagram
wr s= ws
Rankine Cycle with superheat Sometimes called Hirn Cycle
Superheater B
B'
T Turbine
B' A
B
Shaft
A
Boiler
E D C'
D
E
Pump
C'
Condenser
S
Energy Rankine cycle + superheat B' H B
A C' C E S D
Hot reservoir
q c =q boilerq superheater=h B−h Dh B ' −h B=h B '−h D
The reheat cycle Double stage expansion in double stage turbines Superheat again before the second expansion Superheater
re-superheater
T
B
B'
B'
B'' A
A
B
Boiler
E
C'
C'
C'' D
C''
D
E
Pump
Condenser
S
Energy
B''
B'
Hot Reservoir
H B
E – B' + C' – B'' C' C''
A
Turbine B' - C' + B'' – C''
E S D
The regenerative cycle Extract a fraction of the vapor before complete expansion Partially heat the feeding water with that vapor B
Superheater
T
B'
C'
B'
A
A
B C'
E'
boiler E'
C'
E
Mixer (feed heater)
C'' D
Pump E
D
pump
C''
Condenser
S
Regenerative cycle (continued)
B' H B
C'
C'' A
E'
E D S
Back-pressure turbine Exhaust at high pressure Hence at high temperature
Combined Heat and Power (CHP) Or cogeneration
B' H
Heat B
C'
While
C'' A
q=h D ' −h C' q=h C '' −h D
would not be usable
E'
E D S
usable
Primary energy sources At the boiler: ●
● ● ● ●
Traditional Nuclear Oil Coal Natural gas
●
Renewable
Solar (concentration) ● Geothermal ● Biomass ● Waste enhancement ●
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