chemical physics of discharges - Argonne National Laboratory
chemical physics of discharges - Argonne National Laboratory chemical physics of discharges - Argonne National Laboratory
\ 36 3 ' h, I 26. H. Purnell, Gas Chronatogaphy (John Wiley, N. Y., 1962) pp. 371-3. 29. D. ;&shall, P. Jeffers, S. H. Ba,Jer, Chenistry Dept., Cornell Univ., Ithaca, M. Y., personal comnvAnicaticn, NOV., 1966. 33. 1:. c. Rcbertson and R. N. Pease,.J. Amer. Chem. Soc., &, 1880 (1942). 31. C. A. Goy, D. H. Shaw, arid H. 0. Pritchard, J. Phys. Chein., 9, 1504 (1965). , 32. K. L. Wray, Res. Rept. 104, Avco Everett Res. 'Lab., Everett, Mass. (June, 1961). J , 33. D. R. Bates, A. E. Kingstcn, and'R. W. P. McWhirter, hoc. Roy. Soc. A., 3, , 297 (1962).
THE CONVERSION OF i.iEEIHAiW IN AN ARC REACTOR P. R. Anunann* R. S. Timmons V. Krukonis The conversion of hydrocarbons into other products, namely acetylene, has been of considerable commercial and academic interest during the past fzw decades. Several types of arc devices have been reported for carrying out ?;he pyrolysis of methane. Thermodynanic calculations show that if the acetylene is to be re- covered r'rori an equilibrium chemical mixture, high temperatures in the range of 2000 to 35000K are required, depending on the carbon-hydrogen ratio and the pressure of the system. Furthermore, kinetic considerations indicate that the pyrolysis of methane is fast relative to the decomposi- tion of acetylene, and that there is an optimum reaction time to maximum both the conversion of the methane and the yield of acetylene. The most desireable accomplishment of high temperature methane pyroly- sis would be to effect the endothermic reaction. 2CH4 = C2H2 + 3 H2 High temperature chemical equilibria for the carbon-hydrogen system have been computed by Blanchetl and Bauer and Duff2. Assuming that chemical equilibrium is achieved in an electric arc reactor, the data indicate that the temperature at which the acetylene concentration is a maximum. The kinetics of methane pyrolysis and acetylene decomposition during heating and cooling ultimately determine the yield of acetylene. Anderson and Case3 developed a kinetic model to describe the reactions between arc heated hydrogen and methane. ' Calculations provided information on conditions, such as He/CHI+ ratio, and reaction time, to achieve optimum conversion of methane to acetylene. The analyses indicated that conversion is not sensitive to contact time, within 0.1 and 1.3 milliseconds, and that speed of mixing is the most important parameter. Reactions of methane and hydrogen with carbon vapor produced by an electric arc were reported by Baddour and Blanchetl. In their experiments, high acetylene concentrations of 20 to 40 percent in the product gas were found. In an arc process, the reactions which determine the success of the process occur during the heating step and also during the cooling step. Heating of the reactant may proceed either as it passes through the discharge, or when it mixed with arc-heated gases. Cooling of the high temperature gases is usually carried out quickly, either by contact with cold surfacestop mix- ing with cold fluids. This paper describes an experimental study on the con- version of methane which either (1) passed through a confined arc discharge, or (2) was mixed with an arc-heated gas. In this investigation, an attempt was made to understand the factors which affect the extent of methane pyro- lysis ana the yield of acetylene. -c Avco Space Systems Division, 201 Lowell Street, Wilmington, Mass. 01887
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THE CONVERSION OF i.iEEIHAiW IN AN ARC REACTOR<br />
P. R. Anunann*<br />
R. S. Timmons<br />
V. Krukonis<br />
The conversion <strong>of</strong> hydrocarbons into other products, namely acetylene,<br />
has been <strong>of</strong> considerable commercial and academic interest during the past<br />
fzw decades. Several types <strong>of</strong> arc devices have been reported for carrying<br />
out ?;he pyrolysis <strong>of</strong> methane.<br />
Thermodynanic calculations show that if the acetylene is to be re-<br />
covered r'rori an equilibrium <strong>chemical</strong> mixture, high temperatures in the<br />
range <strong>of</strong> 2000 to 35000K are required, depending on the carbon-hydrogen<br />
ratio and the pressure <strong>of</strong> the system. Furthermore, kinetic considerations<br />
indicate that the pyrolysis <strong>of</strong> methane is fast relative to the decomposi-<br />
tion <strong>of</strong> acetylene, and that there is an optimum reaction time to maximum<br />
both the conversion <strong>of</strong> the methane and the yield <strong>of</strong> acetylene.<br />
The most desireable accomplishment <strong>of</strong> high temperature methane pyroly-<br />
sis would be to effect the endothermic reaction.<br />
2CH4 = C2H2 + 3 H2<br />
High temperature <strong>chemical</strong> equilibria for the carbon-hydrogen system have been<br />
computed by Blanchetl and Bauer and Duff2. Assuming that <strong>chemical</strong> equilibrium<br />
is achieved in an electric arc reactor, the data indicate that the temperature<br />
at which the acetylene concentration is a maximum. The kinetics <strong>of</strong> methane<br />
pyrolysis and acetylene decomposition during heating and cooling ultimately<br />
determine the yield <strong>of</strong> acetylene.<br />
Anderson and Case3 developed a kinetic model to describe the reactions<br />
between arc heated hydrogen and methane. ' Calculations provided information<br />
on conditions, such as He/CHI+ ratio, and reaction time, to achieve optimum<br />
conversion <strong>of</strong> methane to acetylene. The analyses indicated that conversion<br />
is not sensitive to contact time, within 0.1 and 1.3 milliseconds, and that<br />
speed <strong>of</strong> mixing is the most important parameter.<br />
Reactions <strong>of</strong> methane and hydrogen with carbon vapor produced by an electric<br />
arc were reported by Baddour and Blanchetl. In their experiments, high<br />
acetylene concentrations <strong>of</strong> 20 to 40 percent in the product gas were found.<br />
In an arc process, the reactions which determine the success <strong>of</strong> the process<br />
occur during the heating step and also during the cooling step. Heating<br />
<strong>of</strong> the reactant may proceed either as it passes through the discharge, or<br />
when it mixed with arc-heated gases. Cooling <strong>of</strong> the high temperature gases<br />
is usually carried out quickly, either by contact with cold surfacestop mix-<br />
ing with cold fluids.<br />
This paper describes an experimental study on the con-<br />
version <strong>of</strong> methane which either (1) passed through a confined arc discharge,<br />
or (2) was mixed with an arc-heated gas. In this investigation, an attempt<br />
was made to understand the factors which affect the extent <strong>of</strong> methane pyro-<br />
lysis ana the yield <strong>of</strong> acetylene.<br />
-c Avco Space Systems Division, 201 Lowell Street, Wilmington, Mass. 01887