Solids and Liquids: Internal Energy and Enthalpy

Both liquids and solids can be considered incompressible substances.  As a result, their specific volume will remain constant during a process.  This means that any energy associated with a volume change is  considered negligible in comparison to other forms of energy.  Due to this fact, the specific heat cp and cv will be equal to each other for a liquid and a solid.  Hence, cp=cv=c.  In turn, this will effect how the internal energy and enthalpy are calculated.

Internal Energy: Solids and Liquids

Similar to an ideal gas, the internal energy of a liquid and solid is dependent on temperature only.  As a result, the partial differential equation in relation to cv will be as follows.

(Eq 1) du=cvdT=c(T)dt

For a process, the change in internal energy from state 1 to state 2 is obtained using the following integration.

(Eq 2) Δu=u2u1=12 c(T)dT  (kJ/kg)

Finally, for small temperature differences, the average specific heat c can be used to determine the change in internal energy.

(Eq 3) Δucavg(T2T1)  (kj/kg)

Enthalpy: Solids and Liquids

Enthalpy is defined by h=u+Pν, where P is the absolute pressure and ν is the specific volume.  For a liquid and solid, the specific volume will be constant.  As a result,  the differential equation for enthalpy change of a liquid and solid is the following.

(Eq 4) dh=du+νΔP+Pdν=du+νdP

where Pdν0

After integrating equation 4, the following equation will result.

(Eq 5) Δh=Δu+νΔPcavgΔT+νΔP (kJ/kg)

Regarding solids, only the term νΔP can be considered insignificant.  As a result, Δh=ΔucavgΔT.  On the other hand, for liquids, there are two common cases that can be encountered.  The first case is when there is a constant pressure during the process, or ΔP=0.  When this is the case, Δh=ΔucavgΔT.  The second case occurs when the temperature is constant during the process, or ΔT=0.  If this is the case than Δh=νΔP.

Finally, if we are trying to find the enthalpy of a compressed liquid, than the following equation is used.

(Eq 6) h@P,Thf@T+νf@T(PPsat@T)

This equation is used when state 1 of a process starts as a saturated liquid.  Than as the process occurs the temperature remains the same until the process ends as a compressed liquid at state 2.

 

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