Why is first TD law different for chemical reactors

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SUMMARY

The discussion centers on the application of the first law of thermodynamics to chemical reactors, specifically Continuous Stirred-Tank Reactors (CSTR). The total change of system energy, represented as ##\frac{\partial E}{\partial \tau}##, is equated to energy transferred via mass flux and internal energy changes. The participants debate the correct interpretation of energy and enthalpy differentials, referencing the derivation from Bird, Stewart, and Lightfoot's "Transport Phenomena" and a specific energy balance derivation. The confusion arises from the placement of the total enthalpy differential in the energy balance equations.

PREREQUISITES
  • Understanding of the first law of thermodynamics for open systems
  • Familiarity with Continuous Stirred-Tank Reactor (CSTR) energy balances
  • Knowledge of enthalpy and its total differential in thermodynamics
  • Experience with mathematical representations of energy transfer in chemical processes
NEXT STEPS
  • Study the derivation of the first law of thermodynamics for open systems
  • Examine energy balance equations specific to CSTRs
  • Learn about the total differential of enthalpy and its applications in thermodynamics
  • Review "Transport Phenomena" by Bird, Stewart, and Lightfoot for comprehensive understanding
USEFUL FOR

Chemical engineers, thermodynamics students, and professionals involved in reactor design and energy balance calculations will benefit from this discussion.

ussername
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I've learned that first thermodynamic law for some open system is in the form of:

Energy+Conservation+Friction+Loss+%28Viscous%29+Mechanical+Work+Heat.jpg

where total change of system energy ##\frac{\partial E}{\partial \tau }## is equal to the transferred heat and work.
Total change of system energy ##\frac{\partial E}{\partial \tau }## is equal to the energy transferred via mass flux (surface integral) plus energy change within the system (volume integral).

Now I've seen energy balance of CSTR reactor and it is in the form of:
tKdm2rH.png


Full derivation is here or here.

I think ##\frac{\partial E}{\partial \tau }## in the bottom picture means total change of system (internal) energy, because further in the derivation it is replaced with total enthalpy differential and it is substituted with CSTR mass balance:
$$\frac{\partial n_{i}}{\partial \tau }=F_{i}^{0}-F_{i}+V\cdot \upsilon _{i}\cdot r_{V}$$
which makes sense only if ##\frac{\partial E}{\partial \tau }## is total change of energy.

If ##\frac{\partial E}{\partial \tau }## in the bottom picture means total change of system energy then it is not the same equation as in the first picture.

Can anybody explain?
 
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I have correctness problems with both the insets in your post, and one of the links. In my judgment and experience, the development that is done correctly is this one: http://jbrwww.che.wisc.edu/home/jbraw/chemreacfun/ch6/slides-enbal.pdf. If you wish to learn more about correctly-done energy balances (both for mechanical energy and thermal energy), see Bird, Stewart, and Lightfoot, Transport Phenomena.
 
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My second picture is from the link you posted.

I had basically problem to understand where to put enthalpy total differential H=f(T,p,n):
$$\frac{\partial H}{\partial \tau}=\dot{H}_{out}-\dot{H}_{in}+\frac{\partial }{\partial \tau}\left (\int_{V}^{ }\frac{\partial H}{\partial m}\,dm \right )$$
First I thought that ##\frac{\partial H}{\partial \tau}## is the total enthalpy change of the system so the total differential H=f(T,p,n) should belong to there.
But the derivation says that total differential belongs to this term:
$$\frac{\partial }{\partial \tau}\left (\int_{V}^{ }\frac{\partial H}{\partial m}\,dm \right )$$and it seems partially logical because this integral adds elements of system enthalpy ##dH## along the system volume, so this integral is equal to the system enthalpy.
 
ussername said:
My second picture is from the link you posted.

I had basically problem to understand where to put enthalpy total differential H=f(T,p,n):
$$\frac{\partial H}{\partial \tau}=\dot{H}_{out}-\dot{H}_{in}+\frac{\partial }{\partial \tau}\left (\int_{V}^{ }\frac{\partial H}{\partial m}\,dm \right )$$
First I thought that ##\frac{\partial H}{\partial \tau}## is the total enthalpy change of the system so the total differential H=f(T,p,n) should belong to there.
But the derivation says that total differential belongs to this term:
$$\frac{\partial }{\partial \tau}\left (\int_{V}^{ }\frac{\partial H}{\partial m}\,dm \right )$$and it seems partially logical because this integral adds elements of system enthalpy ##dH## along the system volume, so this integral is equal to the system enthalpy.
Are you saying that the equations in the second inset you posted are incorrect? Are you familiar with the derivation of the open system (control volume) version of the first law of thermodynamics?
 

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