How Do You Calculate Thermodynamic Quantities for a Compressed Diatomic Gas?

  • Thread starter Thread starter ky92
  • Start date Start date
  • Tags Tags
    Thermodynamics
Click For Summary

Homework Help Overview

The discussion revolves around calculating thermodynamic quantities for a compressed diatomic gas undergoing a reversible adiabatic process. The original poster presents a problem involving a diatomic gas with specific conditions and seeks clarification on various thermodynamic relationships and calculations.

Discussion Character

  • Exploratory, Conceptual clarification, Mathematical reasoning, Assumption checking

Approaches and Questions Raised

  • Participants explore the relationships between internal energy, enthalpy, and heat in different thermodynamic processes, questioning the assumptions made regarding constant pressure and the applicability of specific heat capacities.

Discussion Status

Participants are actively engaging with the original poster's questions, providing insights into the nature of adiabatic and isothermal processes. Some guidance has been offered regarding the use of heat capacities and the implications of different process types, though confusion remains regarding specific calculations and definitions.

Contextual Notes

There is an ongoing discussion about the validity of certain assumptions in the calculations, particularly concerning the nature of the processes involved and the definitions of heat, work, and internal energy. Participants are also referencing external resources for clarification.

ky92
Messages
14
Reaction score
0

Homework Statement


A sample of 3 mol of a diatomic perfect gas at 200K is compressed reversibly and adiabatically until its temperature reaches 250K. Given that Cv,m=27.5 JK-1mol-1, calculate q, w, ΔU, ΔH and ΔS.


Homework Equations


dS = dq/T
ΔU = n(Cv,m)ΔT
ΔH = n(Cp,m)ΔT


The Attempt at a Solution


(skipped the part of q and ΔS)

ΔU = q+w = w
w = -∫PdV = -PΔV = -nRΔT = -1247.2 J
ΔU = -1247.2 J
ΔH = ΔU+Δ(PV) = -2494.4 J

the model answer:
w= ΔU = CvΔT = +4.1 kJ
ΔH = CpΔT = +5.4 kJ


here are my questions:

what's wrong with my answer?
i should not assume Pressure is constant?

if the problem is that Pressure does vary in the process,
why ΔH is still calculated by Cp,m (i know ΔH=q in an isobaric process) ?
why can't i use ΔH = ΔU -w in this case?

is ΔU always equal to CvΔT for isobaric and isochoric process,
and equal to 0 for isothermal process?

Thank You!
i have read my physical chemistry book but i am still confused!
 
Physics news on Phys.org
Well, you'll first have to understand that an adiabatic process is a process where all 3 of the basic Thermodynamics variables change. This means that Temperature,Pressure and Volume are all subset to changes , yet since this process is adiabatic, there is no exchange of Heat Q between the gas and the rest of the system.

You should also understand that Cp and Cv are constants, that you can use when the gas in your problem is ideal/perfect and with a single atom. Cp=5R/2 and Cv=3R/2. When your gas isn't that perfect, there are other values that they take.

ΔU is given by nCvΔT for every reversible process, and you can easily see than in an isothermal process (ΔT=0) ΔU=0.

I am not sure about Entropy or Enthalpy since my memories of that are quite blurry (+ we were not taught of them in school, so..) I hope I have helped you understand some things, if others find mistakes in my explanations feel free to correct me.
 
thank you karkas.

actually you remind me of another question,

for isothermal process,
ΔT=ΔU=0
ΔH = ΔU + Δ(PV)
= ΔU + Δ(nRT)
= 0+0 = 0

so for isothermal process, heat is not necessarily be zero but ΔH is always zero,
while an adiabatic process, heat must be zero while ΔH can be nonzero,
am i right?anyway i am really confused by the equations...
 
Really, the Second Law of Thermodynamics explains it all fairly easily, no need to be confused :)

1)Q=ΔU+W (in an isothermal ΔU=0) and so Q=W=nRT lnΔV. <-- Isothermal
2)Q=ΔU+W (Q=0) => ΔU = - W = - Δ(PV)/1-γ <--- Adiabatic

So indeed in the isothermal : ΔΤ=0 and Q isn't zero.
And in the adiabatic : ΔΤ isn't zero and Q=0.

Anything else?? :) (I hope I am not making mistakes, someone confirm!)
 
why Q=ΔU+W

i know ΔU=q+w and it should be q=ΔU-w
 
http://en.wikipedia.org/wiki/First_law_of_thermodynamics

Does that clear your queries?

@wikiquoting@

Notice that a lot of textbooks (e.g., Greiner Neise Stocker) formulate the first law as:

dU=\delta Q+\delta W\,

The only difference here is that δW is the work done on the system. So, when the system (e.g. gas) expands the work done on the system is − PdV whereas in the previous formulation of the first law, the work done by the gas while expanding is PdV. In any case, both give the same result when written explicitly as:

dU=\delta Q-PdV\
 
i see!
thanks a lot

and could anyone answer my first question posted above...thanks
 
hey could anyone help?
 
Your first question being "what's wrong with my answer?"? It's calculated assuming an isobaric process, which this isn't.
 
  • #10
why would the model use ΔH = CpΔT if it is not an isobaric process?
i thought q=CvΔT and ΔH=q=CpΔT in isobaric process!
 
  • #11
\Delta U=C_V\Delta T and \Delta H=C_P\Delta T always hold for an ideal gas. But \Delta H=Q only for reversible isobaric processes (because dH=T\,dS+V\,dP=q+V\,dP)
 
  • #12
thx!

do u mean that ΔH=CpΔT even in an isochoric process??

so,
for an isothermal process, ΔH=CpΔT = 0
for an isochoric process, ΔH=CpΔT
for an isobaric process, ΔH = Q= ΔU+Δ(PV)=CpΔT in reversible isobaric process

am i correct?
oh my god
so confusing
 
  • #13
Yes, this is true (and confusing). It may help to note that enthalpy is a state variable and therefore process-independent. Thus, if ΔH=CpΔT holds in one process then it holds in all processes (ideal gas only, though).

(Is LaTeX down on PF? I thought maybe things were screwed up on my end.)
 
  • #14
oh this really helps me a lot
thank you!
 

Similar threads

  • · Replies 4 ·
Replies
4
Views
3K
  • · Replies 6 ·
Replies
6
Views
2K
Replies
2
Views
2K
Replies
7
Views
4K
  • · Replies 2 ·
Replies
2
Views
2K
  • · Replies 11 ·
Replies
11
Views
5K
  • · Replies 12 ·
Replies
12
Views
5K
Replies
5
Views
3K
Replies
3
Views
3K
  • · Replies 3 ·
Replies
3
Views
2K