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chemical physics of discharges - Argonne National Laboratory

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358<br />

Ccxposition at the Assumed Freezing Point. The validity <strong>of</strong> this freezing<br />

approacn can be found comparing the predicted composition at the freezing temperature<br />

witc the sbserved composition <strong>of</strong> tne quznched gas stream. The follcwing<br />

variaoles are defined for Table 11, whlcn facilitates the comparison.<br />

For the equilibrium calculatians let the input stoichiometry be charac-<br />

terized by the molar ratio CHq] /[N2 , set equal to + ; let nN21be the<br />

number <strong>of</strong> moles <strong>of</strong> N;1 intro6uced; ani let n: be the number <strong>of</strong> moles OP<br />

species i present at equilibrium 2t a pressure, P, and a temperature, T .<br />

Then Tf is establisned for a given and P, as the temperature at which<br />

equilibrium predicts the quantity nlCN/nN2 is a maximum.<br />

Table I1 shows the mole fraction <strong>of</strong> the predominant species for a Tf value<br />

found in an equimolar input stoichiometry. As mentioned in the "Plasma Composition"<br />

section, above, solid-carbon formation may be retarded in this system. Therefore,<br />

a second set <strong>of</strong> mole fraction data have been presented in Table I1 which<br />

excludes the species C(s) from the calculation.<br />

Table I1<br />

Calculated Equilibrium Composition at the Temperature<br />

where HCN Yield is Maximized<br />

Pressure - 380 torr - 4 P [CHJ+]/ [Np] = 1.0<br />

x2<br />

*e<br />

HC N<br />

0.421<br />

0.252<br />

0.097<br />

others 0.030<br />

Including C( s)<br />

Mole Fractions<br />

0.543<br />

0.283<br />

0.109<br />

0.038. 0.065<br />

0.144 -<br />

0.020<br />

0.497<br />

0.266<br />

0.120<br />

0.073<br />

0.025<br />

0.005<br />

Note a: Adjusted to allow for the reactions: C2H + H - C2%, 2H - h.<br />

0.522<br />

0.274<br />

0.124<br />

0.080<br />

-

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