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The Branching Chain Explosion Upper and Lower Limits

The Branching Chain Explosion Upper and Lower Limits [Pg.440]

The model presented for a thermal explosion predicts that for a reaction mixture of fixed composition and fixed initial temperature, there will be a critical pressure above which explosion will occur and below which a normal stationary reaction will take place. The relation between the critical pressure and temperature is given by a modified Arrhenius equation with a negative temperature coefficient [Eq. (XIV.3.8)] which is [Pg.440]

Systems showing the characteristic of a branching chain explosion (e.g., oxidation of P4, PH3, NH3, H2, etc.) exhibit critical explosion limits of the [Pg.441]

The actual rate of reaction as a function of total pressure at fixed composition and fixed temperature is illustrated in Fig. XIII.3. In the draw- [Pg.442]

It is generally found that the first explosion limit of a branching chain is shifted to lower pressures by the decrease of surface/volume ratio (for example, a system becomes more explosive in larger vessels) or by the addition of an inert gas (for example, N2 or Ar). While the surface/volume behavior is similar to that found in thermal explosions, the effect of added [Pg.442]




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Branched chain

Branched chain explosions

Branching chain explosions

Chain branching

Explosion chain

Explosion limit

Explosion lower

Explosion upper

Explosive limits

Explosivity limits

Lower Explosion Limit

Lower explosive limit

Lower upper

Upper Explosion Limit

Upper Limit

Upper explosive limit

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