chemical physics of discharges - Argonne National Laboratory
chemical physics of discharges - Argonne National Laboratory chemical physics of discharges - Argonne National Laboratory
In experiments on the direct conversion of methane, the reactant was psssed through a confined arc discharge and quenched by mixing hydrogen or helium at several different quench to methane flow ratios. The net enthalpy Of the gas from the arc discharge varied between 78 and 150 kca$ per gram mole which correspond to equilibrium temperatures of 2500 to 33000K. The conversion of methane, that was observed, varied from 65 percent at the low enthalpy to 85-100 percent at the high enthalpy. With a helium quench, the methane conversion varied between 90 and 98 percent, but at low He/CH4 ratios, a large fraction of the methane went to carbon black, due principally to lower quenching rates and greater acetylene decomposition. Methane conversion was slightly lower with a hydrogen quench and the latter probably affected the kinetics of methane decomposition. The conversion of methane by mixing with arc-heated hydrogen was studied in a plug-flow type reactor. Hydrogen was passed through a confined arc discharge. Islethane was mixed with the hydrogen leaving the arc zone, and heated and reacted as the gases flowed co-currently through a cooled pipe., The conversion of the methane was correlated with the enthalpy of the hydrogen arc gas. Conversions were low (15-20 percent) at low enthlpies, and were nearly complete at high enthalpies (go-100 percent). These energies corresponded to 50-60 kcal per mole of methane at the low enthalpies to 220 kcal at high values, and were very Large for the degree of methane reaction. Two effects were important. The arc gas lost energy to the cool reactor walls and the rate of energy transfer decreased with time due to a decrease in the energy driving force. By allowing for energy losses, the conversion was correlated and fair agreement was obtained between the data from (1) cracking methane in the arc discharge, (2) cracking methane in an arc-heated hydrogen stream, and (3) the experbents of Anderson and Casel. The yield of acetylene was also observed to be a function of the available energy, and under sane conditions, acetylene yields of go to 100 percent& theoretical were achieved. References 1. Blanchet, J. L.,"Reactions of Carbon Vapor with Hydrogen and with Methane in a High Intensity Arc, " Sc. D. Thesis, M.I.T., June, 1963. 2. Bauer, S. H., and Duff, R. E., The Equilibrium Composition of the C/H System At Elevated Texperatures, LA-2556, Los Alamos Scientific Labora- tory, Los Alamos, N. M., September 18, 1961. 3. Anderson, J. E., and L. K. Case, An Analytical Approach to Plasma Torch Chemistry, 1, 3, 161-165 (1962).
_r 333 THERMAL CRACKING OF LOW-TEMPERATURE LIGNITE PITCH John S. Berber, Richard L. Rice, and Delmar R. Fortney ' U. S. Department of the Interior, Bureau of Mines, Morgantown Coal Research Center, Morgantown, West Virginia INTRODUCTION The tar used in this study was produced by the Texas Power & Light Company from a Texas lignite carbonized at about 500" C in a fluidized bed. The pitch, as used in this research program, is the tar distillation residue boiling above 350" C. This pitch is about 40 to 50 percent of the crude tar. Pitch is a complex resinous mass of polymerized and polycondcnsed compounds (1). It is an amorphous solid material and quite brittle at room temperature. Tce pitch analyses average 84 percent carbon, 8 percent hydrogen, 5 percent oxygen, and 1 percent each oi nitrogen and sulfur. It is chemically similar to the tar from which it is prepared, .being mainly mixtures of the higher homologs of the compounds contained in the distillable fractions of the tar. The pitch is potentially useful as a binder in the manufacture of products such as roofing cement, metallurgical electrodes, asphalt paving, and pitch fibre pipe, if its characteristics can be modified by physical and chemical techniques to approximate those ol. asphalt and bituminous binders (2). Researchers of the Bureau of Mines, U. S. Department of the Inter.ior, have investigated three methods for changing the lignite pitch characteristics. Air-blowing, which is used successfully to treat bituminous pitch by lower- ing the hydrogen content and increasing the softening point and the penetrability, was not too effective with lignite pitch (1, 2). -- Catalytic dehydrogenation (a) was found to be effective in reducing the hydrogen content of the pitch, but catalyst cost per pound of treated pitch is high, and the catalyst recovery cost would be prohibitive. Thermal cracking has proven to be the most effective in changing the pitch characteristics. This' report covers the preliminary work done on thermal cracking of pitch and shows the variety of products that may be obtained. Thermal cracking is widely used in the petroleum industry, particularly for the production of olefins. Thermal cracking has also been used in the treatment of coal tar.(A, ?), but seldom has been used in the treatment of pitch. The successful treatment of pitch by this process could upgrade the pitch into metallurgical coke, binders, oxidation feedstock for phthalic and maleic anhydrides, and gases such as hydrogen, methane, and ethylene. The binding ability of the cracked pitch and oil distillation.pitch can be determined by the quality of metallurgical electrodes produced using the pitches as binders. Many factors affect the binding properties' of the materials being
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In experiments on the direct conversion <strong>of</strong> methane, the reactant was<br />
psssed through a confined arc discharge and quenched by mixing hydrogen or<br />
helium at several different quench to methane flow ratios. The net enthalpy<br />
Of the gas from the arc discharge varied between 78 and 150 kca$ per gram<br />
mole which correspond to equilibrium temperatures <strong>of</strong> 2500 to 33000K. The<br />
conversion <strong>of</strong> methane, that was observed, varied from 65 percent at the low<br />
enthalpy to 85-100 percent at the high enthalpy. With a helium quench, the<br />
methane conversion varied between 90 and 98 percent, but at low He/CH4 ratios,<br />
a large fraction <strong>of</strong> the methane went to carbon black, due principally to lower<br />
quenching rates and greater acetylene decomposition. Methane conversion<br />
was slightly lower with a hydrogen quench and the latter probably affected<br />
the kinetics <strong>of</strong> methane decomposition.<br />
The conversion <strong>of</strong> methane by mixing with arc-heated hydrogen was studied<br />
in a plug-flow type reactor. Hydrogen was passed through a confined arc discharge.<br />
Islethane was mixed with the hydrogen leaving the arc zone, and heated<br />
and reacted as the gases flowed co-currently through a cooled pipe., The conversion<br />
<strong>of</strong> the methane was correlated with the enthalpy <strong>of</strong> the hydrogen arc<br />
gas. Conversions were low (15-20 percent) at low enthlpies, and were nearly<br />
complete at high enthalpies (go-100 percent). These energies corresponded to<br />
50-60 kcal per mole <strong>of</strong> methane at the low enthalpies to 220 kcal at high values,<br />
and were very Large for the degree <strong>of</strong> methane reaction. Two effects<br />
were important. The arc gas lost energy to the cool reactor walls and the<br />
rate <strong>of</strong> energy transfer decreased with time due to a decrease in the energy<br />
driving force. By allowing for energy losses, the conversion was correlated<br />
and fair agreement was obtained between the data from (1) cracking methane in<br />
the arc discharge, (2) cracking methane in an arc-heated hydrogen stream, and<br />
(3) the experbents <strong>of</strong> Anderson and Casel.<br />
The yield <strong>of</strong> acetylene was also<br />
observed to be a function <strong>of</strong> the available energy, and under sane conditions,<br />
acetylene yields <strong>of</strong> go to 100 percent& theoretical were achieved.<br />
References<br />
1. Blanchet, J. L.,"Reactions <strong>of</strong> Carbon Vapor with Hydrogen and with Methane<br />
in a High Intensity Arc, " Sc. D. Thesis, M.I.T., June, 1963.<br />
2.<br />
Bauer, S. H., and Duff, R. E., The Equilibrium Composition <strong>of</strong> the C/H<br />
System At Elevated Texperatures, LA-2556, Los Alamos Scientific Labora-<br />
tory, Los Alamos, N. M., September 18, 1961.<br />
3. Anderson, J. E., and L. K. Case, An Analytical Approach to Plasma Torch<br />
Chemistry, 1, 3, 161-165 (1962).