Skip to main content

Thermodynamics - Lecture - 11 - Unit - 3 - Steam Properties and Problems

Problem: 1 

A vessel of volume 0.04 m3contains a mixture of saturated water and steam at a temperature of 250°C The mass of the liquid present is 9 kg. Find the pressure, mass, specific volume, enthalpy, entropy and internal energy.

Given data:

V=0.04m3

T= 250°C

m1= 9 kg

To find:

p, m, v, h, S, and U

 

Solution:

From Steam Tables corresponding to 250°C,

vf=v1 = 0.001251 m/kg

Vg = Vs = 0.050037 m/kg

p= 39.776 bar

 

Total volume occupied by the liquid,

V1= m1 v1 = 9 x 0.001251 = 0.0113 m3

Total volume of the vessel,

V = Volume of liquid + Volume of steam V1+Vs

Vs=0.0287 m3

 

Mass of steam, ms = Vs / Vs  =0.0287 / 0.050037

=0.574 kg

Mass of mixture of liquid and steam,

m=m1+ms = 9+ 0.574 = 9.574 kg

 

Total specific volume of the mixture,

v = V / m  = 0.04 /9.574 = 0.00418 m3/kg

 

We know that, v=vf+x Vfg

Vfg = vg - vf

0.00418 = 0.001251 + x (0.050037 -0.001251)

x=0.06

 

From Steam Tables corresponding to 250°C,

hf=1085.8 kJ/kg; hfg=1714.6 kJ/kg

Sf= 2.794 kJ/kg K; sfg = 3.277 kJ/kg K

Enthalpy of mixture,

h=hf+x hfg=1085.8 +0.06 x 1714.6 = 1188.67 kJkg

Entropy of mixture,

s = Sf+x Sfg =2.794 +0.06 x 3.277=2.99 kJ/kg K

Internal energy, u=h-pv

= 1188.67 – 39.776 x 102 x 0.00418 = 1172 kJ/kg

 

Problem 2

3 kg of steam at 18bar occupy a volume of 0.2550m3. During a constant volume the heat rejected is 1320KJ. Determine final internal energy and find initial dryness and work done.

Given data:

V1 =  0.255m

P1 = 18 bar

m = 3kg

Heat rejected, Q =- 1320kJ

Solution:

Specific volume, v1 = V1 / m = 0.255 / 3 = 0.085 m3 / kg

From Steam Tables, corresponding to 18 bar,

hf1 = = 884.5 kJ/kg;

hfg = 1910.3 kJ/kg

sf1 = 2.398kJ/kgK;  sfg = 3.977 kJ/kgK

Vg10.11033 m/kg

0.085 = x1*0.11033

x1 = 0.77

h1 = hf1 + xhfg1 = 884.5 +0.77 x 1910.3 = 2355.43 kJ/kg

s1=sf1+xsfg1

= 2.398 +0.77 x 3.977 = 5.46 kJ/kg

For constant volume process,

V1 = v2 and W=0

By first law of thermodynamics,

Q=U

Heat transfer, Q = U2 –U1

= m[ U2 – (h1 – p1v1)]

1320 = 3 [U2 – (2355.43 – 18 x 100x0.085)

= 2642.43 KJ/Kg

 

 

Problem: 3

Steam initially at 0.3MPa, 250°C is cooled at constant volume. At what temperature will the steam become saturated vapour? What is the steam quality at 80°C.  Also find what is the heat transferred per kg of steam in cooling from 250°C to 80°C.

Given data:

P1= 0.3MPa = 3 bar

T1 = 250°C

T2 =80°C

To find:

T'2, X2 and Q.

Solution:

From Steam Tables (in super heated region),

At 3 bar and 250°C

V1= 0.7964 m3/kg

h1 = 2967.9kJ/kg

For constant volume process, v1 = v’2 = v2

But, v’2 = vg2 = 0.7964 m3/kg

Corresponding to vg2 = 0.7964 m3/kg, from saturated table, the saturation temperature can be noted down.

 

The saturated vapour temperature, T'2 = 122.93°C

 

We know that v2 = v2 + x2 vfg2

where vi = V2

0.7964 = 0.001029 + x2 * (3.4091 - 0.001029)

X2 = 0.2334

 

From saturated table at 80°C

hf2 = 334.9 kJ/kg

hfg2 = = 2308.9 kJ/kg

h2 = 334.9+0.2334 x 2308.9 = 873.8 kJ/kg

According to first law of thermodynamics,

Work, W = Heat, Q + Internal energy, U

Heat transfer, Q=- U here, work, W=0 for constant volume process

= m (u1 - u2)

But, h= u + pv

Heat transfer, Q = (h2 - p2V2) - (hı-PIVI)

= (h2-hi) - (p2V2-P1VI)

= (h2-hi) - Vi (P2-P1) [: V1 = v2 for constant volume process]

= (873.8–2967.9) - 0.7964 (47.36-300) here Psat at 80°C = P2

=-1892.897kJ/kg

 

Problem 4

Ten kg of water of 45°C is heated at a constant pressure of 10bar until it becomes superheated vapour at 300°C. Find the changes in volume, enthalpy, internal energy and entropy.

 

Given data:

m= 10 kg

P1= P2 = 10 bar

T2 = 300°C

 

To find

 ΔV.  Δh,  ΔS and  ΔU

 

Solution:

From Steam Tables, corresponding to 45°C,

h1, hf1 = 188.4 kJ/kg

s1=sf1 = 0.638 kJ/kg K

 

v1 =  Vf1= 0.001010 m./kg;

From Steam Tables, corresponding to 10 bar and 300°C,

Cycle

s2 = 7.125 kJ/kg K;

v2 = 0.258 m3/kg;

h2 = 3052.1 kJ/kg;

Change in volume,   Δ v = m (v2 - v1)

10 (0.258 – 0.001010) = 2.5699 m Ans.

Change in volume,  Δ h=m (h2 – h1)

= 10 (3052.1 - 188.4) = 28637 kJ Ans.

Change in entropy, Δ S = m (s2 - s1)

= 10 (7.125 -0.638) = 64.87 kJ/K

Ans.

Change in internal energy,

Δ U= m (U2 - U1)

= m [(h2 – h1) - (p2v2 – P1v1)

= m[(h2 – h1) – P1 (v2 - v1)        [p1=p2]

= 10[(3052.1-88.4) - 1000(0.258 -0.001010)]

= 26067.1 kJ

 

Comments

Popular posts from this blog

Thermodynamics - Lecture - 10 - Unit - 3 - Steam Properties and Steam Power

  Properties of Pure Substances If any two independent intensive properties of a simple compressible system are defined, other properties automatically assume definite values.  These properties can be expressed in terms of charts, tables or equations. This chapter covers the charts and tables of properties of steam. Pure Substances Substances   of fixed chemical composition are known as pure substances    Example : Water, Helium, Nitrogen, Oxygen etc. Substances exist in any one of the three phases namely solid, liquid and gas. For example, H 2 O may exist in the form ice (solid), Water (Liquid) or Steam (Gaseous). In all these phases it will have the same chemical composition. A   Mixture of two or more phases of a pure substance should also be regarded as pure substance. If Water and Steam Co-exits in a container, the chemical composition of both the Vapour and liquid phases will be identical. Hence this heterogeneous system is also a pure...