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chemical physics of discharges - Argonne National Laboratory

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I<br />

I<br />

t<br />

I,<br />

'\<br />

I<br />

'a<br />

downstream from the discharge to ensure proper dispersal <strong>of</strong><br />

spray in the electrode gap. The C-type reactor employed a<br />

pair <strong>of</strong> rectwar electrodes so set in the gas flow as to<br />

avoid reactant by-passing. "ne use <strong>of</strong> D.C. power,<br />

necessitated stabilization <strong>of</strong> the discnarge by means <strong>of</strong> a<br />

resistive load in the electrical circuit. Provision was<br />

made to admit liquid spray into the inlet gas stream using<br />

the same aerosol generator used in tile type-B reactors.<br />

Table 1.<br />

Reactor units employed.<br />

Type<br />

Reactor Flow Area Discharge Discharge Uilectic<br />

CoGe cm 2<br />

I idth rjarr ie r<br />

cm c1n cm<br />

Tubular 81<br />

Centrifwal A2<br />

Fi3.m ileactor A3<br />

A4<br />

2.203<br />

II<br />

II<br />

n<br />

1.270<br />

0.254<br />

0.127<br />

0.040<br />

2.798<br />

0.560<br />

0.280<br />

0.089<br />

0.15875<br />

II<br />

II<br />

II<br />

rubular<br />

Spray Reactor<br />

B1<br />

62<br />

1.089<br />

II<br />

la270<br />

0.254<br />

1.383<br />

0.277<br />

It<br />

II<br />

Used<br />

Reactor<br />

c1 1.4U 0- 635 0.896 0<br />

"O1Y "hicme ss<br />

gmJLTs:.<br />

Hydrazine yields for the various reactor geometries and<br />

the operating variables employed are given in Figs. 2 tm 6.<br />

From the data presented in rig 2 to 4, it is evident that the<br />

yield varies inversely as an exponential function <strong>of</strong> the<br />

*lower density at pressures under l0Umm <strong>of</strong> mercury. The effect<br />

<strong>of</strong> pressure also follows a Regative exponentid variation<br />

therefore a general equation <strong>of</strong> the form<br />

Y = a exp (-W-cv)<br />

adequately describes the results. Of course this correlation<br />

<strong>of</strong> the results does not in any sense give a complete<br />

description <strong>of</strong> the underlying pnysical chemistry involved in<br />

the synthesis. Ideally,it would have been preferable to<br />

develop separate rate equations in terms <strong>of</strong> the partial<br />

pressures <strong>of</strong> tne various components in the overall hydrazine<br />

1 synthesis. This would have necessitated a complete product<br />

analysis and since,in the present case,these data are lacking<br />

the phenomenological approach had to be used. The constants<br />

the equation for tne various reactors acd operating<br />

conditions used were evaluated using the method <strong>of</strong> least<br />

squares (12). These are tabulated in Table 2. It should be<br />

noted in this Table tnat certLin pressure exponential values<br />

were bracketed. here the relevant data were lacking for<br />

c&cdat&n and ,therefore, the dependence <strong>of</strong> energy yield upon<br />

preesurefdeactors A2 to A4 and B2 were assumed to be the<br />

eane RS those found experimentally for Reactors Al and B1.

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