In accordance with the changes in the free energies of formation of hy
drocarbons as a function of temperature, methane is unstable in terms
of its elements from 530 degrees C, but remains the most stable of hyd
rocarbons up to 1030 degrees C. Using methane, it is necessary to reac
h temperatures of 1200 and 1300 degrees C to produce, respectively, ac
etylene and ethylene. However, since acetylene becomes the most stable
hydrocarbon from 1230 degrees C, it is acetylene that predominates si
t this temperature. According to the variation in the enthalpies of fo
rmation as a function of temperature, the pyrolysis of methane demands
a very high energy input to form primarily acetylene. We calculated t
he composition of a mixture CH4, C2H4, C2H2, C6H6 and H-2 at thermodyn
amic equilibrium by minimizing the Gibbs energy of this system. This m
ethod does not require prior knowledge of the chemical reactions takin
g place at equilibrium. The calculation parameters are the initial H/C
ratio, the temperature, the pressure and the Gibbs energies of each s
ubstance. The analysis of the complex chemical equilibria helps to ide
ntify temperature zones corresponding to stability domains of certain
molecules. Below 1200 degrees C, the disappearance of methane is sligh
t, and the main hydrocarbon produced is benzene, followed by ethylene,
without any significant formation of acetylene. Species with acetylen
ic structures (like C2H2) appear above 1200 degrees C, as well as C2H,
C3H and radicals such as H and CH3. This means that the C-C and C-H b
onds split above 1200 degrees C. The species present have an increasin
gly small H/C ratio, and the initial hydrogen is found virtually in mo
lecular form. The presence of hydrogen in the reaction medium has the
effect of increasing the proportion of the hydrogen-rich species, chie
fly CH4 and C2H4, and of decreasing the conversion of methane. (C) 199
7 Elsevier Science Ltd.