chemical physics of discharges - Argonne National Laboratory

chemical physics of discharges - Argonne National Laboratory chemical physics of discharges - Argonne National Laboratory

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359 \ Frozen Compositior: Calcillation v5rsus Expcri;:icntally. 0bscrvt.d Ccwposition. IC, indeed, the oriSinal assuption that important reactiotis occurrirg in the gas ' withdrawn from the plasma into the cold quenching tube are .frozen.in ths vicinity 1 1 ,of 3000 K is, valid, then agree'ment should be found betveeri the cc::!pssitions listed in Tables I and 11. Ir. comparing the argon-fret coinposition listed in Table I with PO~UIM 2 in Table 11, rciatively $cod agrement is found. This comparison has been extended to thc' ikll ranee of stsichiomctries studied. i)n Fig. 4, the maximum nitrogen'conversion, amar-l , and am0,-2, has been plotted ' against input CH)+/N2-molc ratio, 4,. The s.dlscript 1 refers to calculations includ- ' ing C(s); subscript 2, to excludine, C(s). Agrceinunt between the freezing mcdel and crbserved results is very good over more than a two-decade range in stoichiometry variation. These results strongly support .the freezing model in the overall reac- ; tion path. With the existing scatter of the data, a delineation between the single-phase and two-phase equilibrium predictions of composition at Tf is not possible. Additional sxperimental runs may lessen this ambiguity. The retarda- / tion of carbon solid fcrmation, however, accoiints fur Less than a 10 percent change in predicted maximum nitrogen conversion, an the average. Freezing Temperature. The data do not allow an t.xact determination of a frcczing temperature appropriate to the quenching process. keferring back to Fig. 3a, a change of a few hundred degrees in the assumed Tf could account for the data points which indicate 10 to 20 percent less than the two-phase equilibrium predictions of maximum nitrogen conversion. Fig. 3b shows the HCN concentration plateaus to be quite broad. Hence the nitrogen conversion prediction would be relatively insensitive to variation in freezing temperature over the range from 1500 to 3000 K. Future experimental refinenents may allow a mvre exact determination of Tf . Observed Compositions in Nitrile Experiments. An analysis of the maximum nitrugen convcrsion predicted by tiiernochenical equilibrium has not been nlade fi.r the different nitrile inputs desckibed in tne "Expcrirnental Conditions'' zectiuri. The similarity cjf .product ciistri!iiition and uf the rxtio of. HCN to !Q in the prcduct poitito to the same reaction mechanisms as iii tile CiU+/l\I2 studics. Correlatiuri with Studies by Other Investigators If the proposed reaction mechanism is correct, then the yields found in other studies of the synthesis of HCN by thermal reactions of hydrocarbons with riitrogeri should not exceed the predicted values of a . Some results of the production of HCN in plasma jets have been reported, as was mentioned in the "fieviolis Studies" section. While the differences in design between the plasma jet and induction plasma reactors are not detailed here, sample results from these other studies are plotted on Fig. 4. The maximum nitrogen conversion vdues observed 'in the nitrogen plasma jet experiments of Leutnerll (designated XL) and FreemanE (designated xF ) appear. These experimental data points are seen to lie below the maximum nitrogen conversion prediction. I

360 The phenomena ir. t:te pias::.& ::et experiments which convert less nitrogen than the ,;axinurn pred3ct.Yd 6). the ?'re:czilig rnuuel my well be l.ir,ked to a [nixing or diff'L;sian rate (CHq a:. i 32 were !~dt prcfliixta) or' tc temperatures 4nsur'ficient to reach Thi;.qsesticn is ~ i ~ sub,).:et l : 12 a separ-te theoretical analysis now in progress Tf . by the author . THE REACTION SEQUENCE The experimental data support the fallowing description of the overall reac- tion seqdence: i. Plasma Reactic;;w. ' Feed reagerits. are dissociated to their atomic constitu- ents in a therim, plasma. Some Tthermai ioiiizatiQn accurs at sufficiently high ternperatu.-s. CF& i 92 - c + H + N + C+ + H+ + N+ + e- 2. Initial Coohnt Plasma taken inco a small-diameter cold tube rapidly cools witn chemical reactio:is following equlibriwn. C + H + N + ions - H + CIV + C2H + N2 - HCN + @ + N2 + C2w 3. Frozen Reaction Emetics. Rapid cooling continues, but at a rate much greater than the progress of the apparently complex reaction sequence necessary to des%roy trle species HCN, C2H2, and %. Hence the composi- tion of the cooiliig gas is frozen at the end of Step.2. Evidence fyr the Freezing llbdel in Other Reacting Systems. The freezing model , likely is applicable to a wide variety of reacting thermal plasma systems which ' emplcy a rapid quench. hmnann and. Timiinsl5 found a mechanism involving the freezin& of equilibratiag reactiuns 'ta be applicable to their study of the quenching of \ nitrogen-oxygetl plasmc. Ahed by a wealth of published rate data on chemical reactiotis in air, they were ~ble to model thc time-temperature-composition history of M-0 plasma cooling within mail-diameter tubes. A quite similar freezing tempera- 1 ture, Tf , was found at 35Oi;'K 1'c.r that system. The equilibrium composition of nitric uxi?e, NO, at Tf was preserved during continued rapid coolfng. \ CONCLUSIONS ' . , . . \ Mixtures of mechane and nitrogen can be fed continuously to a thermal argon indluctiori plasma maintaified abcve 13,300 K. .A rapid quer.ch of the heated plasma kxture produces HCN, C2@, anc &. the nitrogen converted, range between 3 and 70 percent, a function of the input , Final yields of HCN, expressed'as a fraction Of I stoicbiometry . i 1 I ''; < ti c

359<br />

\ Frozen Compositior: Calcillation v5rsus Expcri;:icntally. 0bscrvt.d Ccwposition.<br />

IC, indeed, the oriSinal assuption that important reactiotis occurrirg in the gas<br />

'<br />

withdrawn from the plasma into the cold quenching tube are .frozen.in ths vicinity<br />

1 1 ,<strong>of</strong> 3000 K is, valid, then agree'ment should be found betveeri the cc::!pssitions listed<br />

in Tables I and 11. Ir. comparing the argon-fret coinposition listed in Table I with<br />

PO~UIM 2 in Table 11, rciatively $cod agrement is found.<br />

This comparison has been extended to thc' ikll ranee <strong>of</strong> stsichiomctries studied.<br />

i)n Fig. 4, the maximum nitrogen'conversion, amar-l , and am0,-2, has been plotted<br />

' against input CH)+/N2-molc ratio, 4,. The s.dlscript 1 refers to calculations includ-<br />

'<br />

ing C(s); subscript 2, to excludine, C(s). Agrceinunt between the freezing mcdel and<br />

crbserved results is very good over more than a two-decade range in stoichiometry<br />

variation. These results strongly support .the freezing model in the overall reac-<br />

;<br />

tion path. With the existing scatter <strong>of</strong> the data, a delineation between the<br />

single-phase and two-phase equilibrium predictions <strong>of</strong> composition at Tf is not<br />

possible. Additional sxperimental runs may lessen this ambiguity. The retarda-<br />

/ tion <strong>of</strong> carbon solid fcrmation, however, accoiints fur Less than a 10 percent change<br />

in predicted maximum nitrogen conversion, an the average.<br />

Freezing Temperature. The data do not allow an t.xact determination <strong>of</strong> a frcczing<br />

temperature appropriate to the quenching process. keferring back to Fig. 3a, a<br />

change <strong>of</strong> a few hundred degrees in the assumed Tf could account for the data points<br />

which indicate 10 to 20 percent less than the two-phase equilibrium predictions <strong>of</strong><br />

maximum nitrogen conversion. Fig. 3b shows the HCN concentration plateaus to be<br />

quite broad. Hence the nitrogen conversion prediction would be relatively insensitive<br />

to variation in freezing temperature over the range from 1500 to 3000 K.<br />

Future experimental refinenents may allow a mvre exact determination <strong>of</strong> Tf .<br />

Observed Compositions in Nitrile Experiments. An analysis <strong>of</strong> the maximum<br />

nitrugen convcrsion predicted by tiiernochenical equilibrium has not been nlade fi.r<br />

the different nitrile inputs desckibed in tne "Expcrirnental Conditions'' zectiuri.<br />

The similarity cjf .product ciistri!iiition and uf the rxtio <strong>of</strong>. HCN to !Q in the prcduct<br />

poitito to the same reaction mechanisms as iii tile CiU+/l\I2 studics.<br />

Correlatiuri with Studies by Other Investigators<br />

If the proposed reaction mechanism is correct, then the yields found in other<br />

studies <strong>of</strong> the synthesis <strong>of</strong> HCN by thermal reactions <strong>of</strong> hydrocarbons with riitrogeri<br />

should not exceed the predicted values <strong>of</strong> a . Some results <strong>of</strong> the production <strong>of</strong><br />

HCN in plasma jets have been reported, as was mentioned in the "fieviolis Studies"<br />

section. While the differences in design between the plasma jet and induction<br />

plasma reactors are not detailed here, sample results from these other studies are<br />

plotted on Fig. 4. The maximum nitrogen conversion vdues observed 'in the nitrogen<br />

plasma jet experiments <strong>of</strong> Leutnerll (designated XL) and FreemanE (designated xF )<br />

appear. These experimental data points are seen to lie below the maximum nitrogen<br />

conversion prediction.<br />

I

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