Modern Control Engineering

(Chris Devlin) #1
108 Chapter 4 / Mathematical Modeling of Fluid Systems and Thermal Systems

where capacitance, lb-ft^2 lbf


mass of gas in vessel, lb


gas pressure, lbfft^2


volume of vessel, ft^3


density, lbft^3


The capacitance of the pressure system depends on the type of expansion process


involved. The capacitance can be calculated by use of the ideal gas law. If the gas ex-


pansion process is polytropic and the change of state of the gas is between isothermal


and adiabatic, then


(4–10)


wheren=polytropic exponent.


For ideal gases,


or


where absolute pressure, lbfft^2


volume occupied by 1 mole of a gas, ft^3 lb-mole


universal gas constant, ft-lbflb-mole °R


absolute temperature, °R


specific volume of gas, ft^3 lb


molecular weight of gas per mole, lblb-mole


Thus


(4–11)


whereRgas=gas constant, ft-lbflb °R.


The polytropic exponent nis unity for isothermal expansion. For adiabatic expansion,


nis equal to the ratio of specific heats cpcv, where cpis the specific heat at constant pres-


sure and cvis the specific heat at constant volume. In many practical cases, the value of


nis approximately constant, and thus the capacitance may be considered constant.


The value of drdpis obtained from Equations (4–10) and (4–11). From


Equation (4–10) we have


or


Substituting Equation (4–11) into this last equation, we get


dr


dp


=


1


nRgas T


dr


dp


=


1


Knrn-^1


=


rn


pnrn-^1


=


r


pn


dp=Knrn-^1 dr


pv=


p


r


=


R



M


T=Rgas T


M=


v=


T=


R



=


v–=


p=


pv=


R



M


pv–=R T



T


pa


V


m


b

n

=


p


rn


=constant=K


r=


V=


p=


m=


C=


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