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Tony's Intertwingled Memex β€’ Reference Manual

Chemical & Aerospace Engineering (Non-Linear Fluids) Solution

Formulas & Definitions

Problem Overview

We calculate the instantaneous rate of pressure change with respect to volume (dPdV\frac{dP}{dV}dVdP​) for a non-ideal gas governed by the Van der Waals equation of state:

(P+V2)(Vβˆ’1)=12(P + V^2)(V - 1) = 12(P+V2)(Vβˆ’1)=12
evaluated at the operational condition V=3Β L/molV = 3\text{ L/mol}V=3Β L/mol and P=5Β atmP = 5\text{ atm}P=5Β atm.


Step-by-Step Mathematical Solution

Step 1: Formally Apply the Product Rule with Implicit Differentiation

The governing equation is the Product Rule:

ddV[uβ‹…v]=dudVβ‹…v+uβ‹…dvdV\frac{d}{dV}[u \cdot v] = \frac{du}{dV} \cdot v + u \cdot \frac{dv}{dV}dVd​[uβ‹…v]=dVdu​⋅v+uβ‹…dVdv​
(This rule is defined in Product Rule and Implicit Differentiation.)

Let u=P+V2u = P + V^2u=P+V2 and v=Vβˆ’1v = V - 1v=Vβˆ’1. Treating PPP as an implicit function P(V)P(V)P(V):

ddV[P+V2]β‹…(Vβˆ’1)+(P+V2)β‹…ddV[Vβˆ’1]=ddV[12]\frac{d}{dV}[P + V^2] \cdot (V - 1) + (P + V^2) \cdot \frac{d}{dV}[V - 1] = \frac{d}{dV}[12]dVd​[P+V2]β‹…(Vβˆ’1)+(P+V2)β‹…dVd​[Vβˆ’1]=dVd​[12]
(dPdV+2V)(Vβˆ’1)+(P+V2)(1)=0\left(\frac{dP}{dV} + 2V\right)(V - 1) + (P + V^2)(1) = 0(dVdP​+2V)(Vβˆ’1)+(P+V2)(1)=0

Step 2: Algebraically Isolate dPdV\frac{dP}{dV}dVdP​

Distribute and group like terms:

(Vβˆ’1)dPdV+2V(Vβˆ’1)+P+V2=0(V - 1)\frac{dP}{dV} + 2V(V - 1) + P + V^2 = 0(Vβˆ’1)dVdP​+2V(Vβˆ’1)+P+V2=0
(Vβˆ’1)dPdV=βˆ’2V(Vβˆ’1)βˆ’Pβˆ’V2(V - 1)\frac{dP}{dV} = -2V(V - 1) - P - V^2(Vβˆ’1)dVdP​=βˆ’2V(Vβˆ’1)βˆ’Pβˆ’V2
dPdV=βˆ’2V(Vβˆ’1)βˆ’Pβˆ’V2Vβˆ’1\frac{dP}{dV} = \frac{-2V(V - 1) - P - V^2}{V - 1}dVdP​=Vβˆ’1βˆ’2V(Vβˆ’1)βˆ’Pβˆ’V2​

Step 3: Substitute Operational Metrics (V=3Β L/mol,P=5Β atmV = 3\text{ L/mol}, P = 5\text{ atm}V=3Β L/mol,P=5Β atm)

dPdV∣(3,5)=βˆ’2(3)(3βˆ’1)βˆ’5βˆ’(3)23βˆ’1=βˆ’6(2)βˆ’5βˆ’92=βˆ’12βˆ’142=βˆ’262=βˆ’13Β atm/(L/mol)\left.\frac{dP}{dV}\right|_{(3,5)} = \frac{-2(3)(3 - 1) - 5 - (3)^2}{3 - 1} = \frac{-6(2) - 5 - 9}{2} = \frac{-12 - 14}{2} = \frac{-26}{2} = -13\text{ atm/(L/mol)}dVdP​​(3,5)​=3βˆ’1βˆ’2(3)(3βˆ’1)βˆ’5βˆ’(3)2​=2βˆ’6(2)βˆ’5βˆ’9​=2βˆ’12βˆ’14​=2βˆ’26​=βˆ’13Β atm/(L/mol)


Engineering Conclusion

At V=3Β L/molV = 3\text{ L/mol}V=3Β L/mol, the rate of pressure drop is βˆ’13Β atm/(L/mol)-13\text{ atm/(L/mol)}βˆ’13Β atm/(L/mol). In rocket combustion chambers and pressure vessels, dPdV\frac{dP}{dV}dVdP​ is directly linked to the isothermal compressibility Ξ²=βˆ’1Vβˆ‚Vβˆ‚P\beta = -\frac{1}{V}\frac{\partial V}{\partial P}Ξ²=βˆ’V1β€‹βˆ‚Pβˆ‚V​. A steep negative derivative indicates that small volume expansions cause rapid pressure drops, providing critical data to design fast-acting injector valves that prevent combustion blow-out or acoustic pressure spikes in liquid rocket engines.