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R. Meyer J. Köhler A. Homburg Explosives

R. Meyer J. Köhler A. Homburg Explosives

R. Meyer J. Köhler A. Homburg Explosives

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Thermodynamic Calculation of Decomposition Reactions<br />

In decomposition processes (detonation in the case of high explosives<br />

or burning processes in the case of gunpowders and rocket propellants),<br />

the kilogram CaHbOcNd is converted into one kilogram<br />

n1 CO2 + n2 H2O + n3 N2 + n4 CO + n5 H2 + n6 NO.<br />

In the case of industrial explosive with a positive W Oxygen Balance,<br />

the occurrence of free oxygen O2, and in the case of explosive with a<br />

very negative oxygen balance, e.g., TNT, the occurrence of elementary<br />

carbon C have to be considered. If alkali metal salts such as NaNo3<br />

are included, the carbonates of these are taken as reaction products,<br />

e.g., Na2CO3. The alkaline earth components, e.g., CaNO3 are assumed<br />

to form the oxides, e.g., CaO; chlorine will be converted into<br />

HCl; sulfur into SO2.<br />

Exact calculations on burning processes in rocket motors must include<br />

dissociation phenomena; this is done on computer facilities (at leading<br />

national institutes*), and the relevant industrial laboratories in this field<br />

are nowadays equipped with computers and programs. The following<br />

explanations are based on simplifying assumptions.<br />

1. Conventional Performance Data of Industrial <strong>Explosives</strong>.<br />

The explosion of an industrial explosive is considered as an isochoric<br />

process, i.e. theoretically it is assumed that the explosion occurs<br />

confined in undestroyable adiabatic environment. Most formulations<br />

have a positive oxygen balance; conventionally it is assumed, that only<br />

CO2, H2O, N2 and surplus O2 are formed. The reaction equation of the<br />

example above is then<br />

C8.19H40.48O37.39N18.73 =<br />

8.19 CO2 + 40.48<br />

2<br />

h2O + 18.73<br />

2 N2 + 1<br />

40.48<br />

(37.39 - 2 x 8.19 -<br />

2 2 )O2 =<br />

314<br />

8.19 CO2 + 20.24 H2O + 9.37 N2 + 0.39 O2<br />

The real composition of the explosion gases is slightly different; CO<br />

and traces of NO are also formed.<br />

1.1 Heat of explosion.<br />

Table 33 also lists the enthalpies and energies of formation of the<br />

explosives and their components.<br />

* The data for the heat of explosion, the volume of explosion gases and specific<br />

energy given in this book for the individual explosives have been calculated<br />

with the aid of the “ICT-Code” in the Fraunhofer Institut für CHEMISCHE<br />

TECHNOLOGIE, D-76318 Pfinztal, including consideration of the dissociation<br />

phenomena. Therefore, the values have been changed in comparison to the<br />

figures listed in the first edition of this book (computed without dissociation).

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