How Do You Calculate Cp and Cv for a Specific Fluid?

  • Thread starter Thread starter Ibn_Nizar
  • Start date Start date
  • Tags Tags
    Thermo
Click For Summary
SUMMARY

This discussion focuses on calculating the specific heat capacities Cp and Cv for a fluid defined by the equations u=196+0.718t and pv=0.287(t+273). The specific heat capacity Cv is determined to be 0.718 kJ/kg·K, while Cp is calculated as 1.005 kJ/kg·K. Additionally, the net work done during the expansion of 2 kg of this fluid from 1 MPa and 100°C to 30°C, with no heat transfer, is found to be 100.52 kJ.

PREREQUISITES
  • Understanding of thermodynamic properties, specifically internal energy and enthalpy.
  • Familiarity with the first law of thermodynamics.
  • Knowledge of differentiation in calculus for thermodynamic equations.
  • Basic principles of fluid mechanics and heat transfer.
NEXT STEPS
  • Study the derivation of specific heat capacities from thermodynamic equations.
  • Learn about the first law of thermodynamics and its applications in closed systems.
  • Explore the relationship between internal energy, enthalpy, and work done in thermodynamic processes.
  • Investigate the properties of specific fluids and their behavior under varying conditions.
USEFUL FOR

Students and professionals in mechanical engineering, thermodynamics, and fluid mechanics who are looking to deepen their understanding of heat capacity calculations and energy transfer in fluid systems.

Ibn_Nizar
Messages
1
Reaction score
0
Hi,

I'm stuck. Can someone help me out?

Problem:
The properties of a certain fluid are related as follows:

u=196+0.718t

pv=0.287(t+273)

(a)where 'u' is the specific internal energy(Kj kg), t is in degress Celsius, p is pressure(Kn/m2) and v is specific volume (m3 kg).For this fluid. Find Cp and Cv

(b)A system composed of 2 kg of the above fluid expands in a frictionless piston and cylinder from an initial state of 1 Mpa, 100degrees Celsius to a final temp of 30degress Celsius.If there is no heat transfer, find the net work for the process.
--------------------------------

This is what i have tried:

in (a), i tried to link the two equations together, so that i could get 'u' and 'pv' in the same equation:

u=196+2.5(pv-78.35)

I'm stuck now.How do i proceed? i know the formula for cp and cv, which is Cp=(do)u/(do)t

cv=(do)Q/(do)T .How do i use these formulas with respect to the above equation?

(b)I'm totally confused on this one. I don't know where to start.All i could understand is to find the work done, and that Q=0.

Thanks.
 
Physics news on Phys.org
Hi, sorry I haven't responded before now.

Ibn_Nizar said:
in (a), i tried to link the two equations together, so that i could get 'u' and 'pv' in the same equation:

u=196+2.5(pv-78.35)

I'm stuck now.How do i proceed?

You should have the following relations handy:

c_v=\left(\frac{\partial u}{\partial T}\right)_P

c_p=\left(\frac{\partial h}{\partial T}\right)_v

You should also know the definition of enthalpy.

(b)I'm totally confused on this one.

Start by writing down the first law for the system.

Q_{NET}+W_{NET}+E_{mass,NET}=\Delta U + \Delta KE + \Delta PE

Now you've already noted that you can set Q_{NET}=0. What else can you set equal to zero? And what else do you know?
 
Hi,
just do these things:
for Ques a)
Cv=du/dt=d(196+0.718t)/dt

after differentiating wrt to t u will get Cv=0.718 Ans

And Cp= dh/dt=d(u+pv)/dt=du/dt+d(pv)/dt
=d(196+0.718t)/dt + d(0.287(t+273))/dt
Cp= 0.718 + 0.287
Cp=1.005 Ans

For Ques b):

dQ=dU+dW as per first law of thermodynaimcs
but as there is no heat transfer therefore dQ=0. So above equation becomes
dW= - dU= - (u2-u1)= u1-u2

at t=100 C, u1= 196+(0.718*100)
& at t=30 C, u2= 196+ (0.718*30)

so dW= u1-u2= 50.26 (By solving above two equations of u1 & u2)

therefore for 2 Kg of fluid dW= 2 x 50.26 KJ = 100.52 KJ Ans
 

Similar threads

  • · Replies 14 ·
Replies
14
Views
9K
  • · Replies 3 ·
Replies
3
Views
3K
  • · Replies 26 ·
Replies
26
Views
7K
  • · Replies 3 ·
Replies
3
Views
2K
Replies
1
Views
3K
  • · Replies 3 ·
Replies
3
Views
5K
Replies
5
Views
5K
  • · Replies 6 ·
Replies
6
Views
3K
  • · Replies 25 ·
Replies
25
Views
5K
  • · Replies 1 ·
Replies
1
Views
18K