For all chambers, initially, the internal volume
of the installation is filled with nitrogen at an initial
gas pressure of p0 = 1 atm and a temperature of T0
= 300 K. The initial velocity of the medium has
zero value. The gas in the receivers is at elevated
pressure values of 10–30 atm, temperature T0 = 300
K, and zero velocity. The jets of oxygen and
hydrogen are directed at an angle to each other for
better mixing of the components. At the initial time
t0 = 0, the valves are removed and the gas flows
from the receivers into the chamber. The detonation
was initiated by the concentrated release of energy
in the mixing zone. It is necessary to determine the
values of the gas parameters in the chamber after
ignition at t > 0.
The geometrical parameters of the installations
and the nature of the boundary conditions make it
possible to model the flow within the framework of
the axial symmetry approximation. The flow of a
viscous heat-conducting compressible medium
inside the chambers was described by non-
stationary two-dimensional Reynolds equations for
the laws of conservation of mass, momentum, and
energy, taking into account the effects of
turbulence. Changes in the mass concentration of
components of a chemically reacting gas mixture
were determined using Fick's second law for
diffusion in multicomponent mixtures. The model
of chemical reactions is based on a two-stage
model of chemical kinetics for the average
molecular weight of a gas, including ignition delay.
The problem posed above was solved numerically
using the large particle method. For verification of
the numerical algorithm and to check solution
stability, test simulations were made for various
sizes of numerical cells using the Fluent program.
The comparison of results shows the reliability of
our study. A detailed mathematical formulation of
the problem can be seen in, [5], [6].
The energy supply to the detonation initiation
chamber should be carried out when, as a result of
turbulent mixing, an area with the necessary
parameters of a combustible gas mixture arises, and
heat generation in the zone of chemical
transformations is mainly determined by the rate of
turbulent mixing of reacting gas components.
Figure 2 shows the cross-section of the
chamber of the first type at time t = 1.4∙10-3 s from
the beginning of the mixture supply to the chamber.
The flow moves from above here, and the output of
combustion products occurs to the right. Note that
at this point in time, there has not yet been a
concentrated supply of energy to initiate
detonation. Nevertheless, due to the complex
geometry of the rigid walls of the channel, "hot
spots" are formed in the boundary layers - local
areas where the gas temperature significantly
exceeds the ignition temperature Tig = 1200 K,
while the bulk of the gas in the chamber remains
quite cold. Such spontaneous ignition of the
mixture disrupts the optimal mode of operation of
the camera and creates technological problems.
Fig. 3: Map of the chemical reaction rate
(kgmoll/(m3 s)) at the instant t = 2.510-3 s.
Let the flow in the chamber of the first type
move in the opposite direction (Figure 3). S1 is the
surface of the exit of combustion products, and S2
is the entrance of reagents into the chamber. Here,
S21 is a slit through which a jet of oxygen enters,
and S22 is a jet of hydrogen. S4 is the axis of
symmetry of the chamber. It can be seen from the
figure that a stagnant zone is formed in the upper
left corner of the chamber, where the nitrogen
concentration decreases slowly. Heat generation in
this zone is low, the turbulent flame practically
WSEAS TRANSACTIONS on FLUID MECHANICS
DOI: 10.37394/232013.2023.18.11