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R. Meyer J. Köhler A. Homburg Explosives

R. Meyer J. Köhler A. Homburg Explosives

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321 Thermodynamic Calculation of Decomposition Reactions<br />

The composition of the reaction products (mol %):<br />

28.63% H2O<br />

28.39% CO<br />

21.07% CO2<br />

4.13% H2<br />

14.63% N2<br />

0.21% O2<br />

0.48% NO<br />

0.37% KOH<br />

1.50% OH<br />

}<br />

0.42% H<br />

dissociated atoms and radicals<br />

0.09% O<br />

0.02% K<br />

2. Rocket Propellants<br />

Raketentreibstoffe; propellants de roquette<br />

The calculation of the performance data of rocket propellants is carried<br />

out in the same manner as shown above for gunpowders, but the<br />

burning process in the rocket chamber proceeds at constant pressure<br />

instead of constant volume. For the evaluation of the heat of reaction,<br />

the difference of the enthalpies of formation instead of the energies<br />

must now be used; for the internal heat capacities, the corresponding<br />

enthalpy values are listed in Table 38 below (instead of the energy<br />

values in Table 31); they are based on the average specific heats cp at<br />

constant pressure instead of the cv values. The first step is to calculate<br />

the reaction temperature Tc and the composition of the reaction gases<br />

(mole numbers n1, etc.). The second step is to evaluate the same for<br />

the gas state at the nozzle exit (transition from the chamber pressure<br />

pc to the nozzle exit pressure pe e.g., the atmospheric pressure). The<br />

basic assumption is, that this transition is “isentropic”, i.e., that the<br />

entropy values of the state under chamber pressure and at the exit are<br />

the same. This means that the thermodynamic transition gives the<br />

maximum possible output of kinetic energy (acceleration of the rocket<br />

mass).<br />

The calculation method begins with the assumption of the temperature<br />

of the exit gases, e.g., Te = 500 K. The transition from the thermodynamical<br />

state in the chamber into the state at the nozzle exit is<br />

assumed to be instantaneous, i.e. the composition of the gases remains<br />

unchanged (“frozen” equilibria). The entropy of the exit gases at<br />

the assumed temperature Te is assumed to be the same as the<br />

entropy of the gases in the chamber (known by calculation); the<br />

assumed value Ta is raised until both entropy values are equal. Since<br />

both states are known, the corresponding enthalpy values can be<br />

calculated. Their difference is the source of the kinetic energy of the

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