Method for checking thermocatalytic sensors of mine safety systems

Claim 1

A method for checking, in a mine environment, a thermocatalytic methane sensor having a gas permeable reaction chamber housing a thermo-catalytic converting element and a supply voltage for controlling the temperature of said thermo-catalytic converting element, comprising the successive steps of: reducing the sensor supply voltage to a level at which said thermo-catalytic converting element is cooled to a temperature obviating methane oxidation thereon; keeping the sensor at the reduced supply voltage for a time at least equal to a period during which methane concentration in said reaction chamber is levelled out to become equal to that in the mine environment; raising the sensor supply voltage, following the levelling out of methane concentration, stepwise to a level at which said thermo-catalytic converting element is heated to a temperature at which methane is oxidized thereon; measuring maximum and steady-state output signals provided by the sensor and also the time constant of a transient process during which the methane concentration changes within said reaction chamber and which continues until a dynamic equilibrium is set up between methane oxidizing on said thermo-catalytic converting element and methane penetrating into said reaction chamber from the mine environment; determining, after said measurements, efficiency of the thermo-catalytic converting element in methane oxidation, resistance of at least a wall of the reaction chamber to diffusive transfer of methane through its walls, and the sensor error in measuring methane concentration on the basis of the following expressions: ##EQU10## where γ is the throughput rate of the thermo-catalytic converting element in m 3 /sec; S H and S y are the maximum and steady-state values of the output signals of said sensor; V K is the volume of the reaction chamber, in cu.m.; T is the time constant of the transient process, in seconds; ##EQU11## where φ is the resistance of said wall of the reaction chamber to the transfer of methane through its gas-permeable walls, in sec/m 3 ; ##EQU12## wherein ΔC is the absolute error in methane concentration measured by the sensor, in vol.%; C is the methane concentration corresponding to the signal S H produced by the sensor, in vol.%; 100is a coefficient for converting the volume concentration of methane from relative units to percentage points; K is a coefficient of conversion of methane flow reacting on said thermo-catalytic converting element to an electric signal being measured, [Bc/m 3 or Ac/m 3 ].

Claim 2

A method for checking, in a mine environment, a thermocatalytic methane sensor having a gas permeable reaction chamber housing a thermo-catalytic converting element and a supply voltage for controlling the temperature of said thermo-catalytic converting element, comprising the successive steps of: reducing the sensor supply voltage to a level at which said thermo-catalytic converting element is cooled to a temperature obviating methane oxidation thereon; keeping the sensor at the reduced supply voltage for a time at least equal to a period during which methane concentration in said reaction chamber is levelled out to become equal to that in the mine environment; raising the sensor supply voltage, following the levelling out of methane concentration, stepwise to a level at which said thermo-catalytic converting element is heated to a temperature at which methane is oxidized thereon; measuring maximum and steady-state output signals provided by the sensor and also the time constant of a transient process during which the methane concentration changes within said reaction chamber and which continues until a dynamic equilibrium is set up between methane oxidizing on said thermo-catalytic converting element and methane penetrating into said reaction chamber from the mine environment; determining, after said measurements, efficiency of the thermo-catalytic converting element in methane oxidation, resistance of at least a wall of the reaction chamber to diffusive transfer of methane through its walls, and the sensor error in measuring methane concentration on the basis of the following expressions: ##EQU10## where γ is the throughput rate of the thermo-catalytic converting element in m 3 /sec; S H and S y are the maximum and steady-state values of the output signals of said sensor; V K is the volume of the reaction chamber, in cu.m.; T is the time constant of the transient process, in seconds; ##EQU11## where φ is the resistance of said wall of the reaction chamber to the transfer of methane through its gas-permeable walls, in sec/m 3 ; ##EQU12## wherein ΔC is the absolute error in methane concentration measured by the sensor, in vol.%; C is the methane concentration corresponding to the signal S H produced by the sensor, in vol.%; 100is a coefficient for converting the volume concentration of methane from relative units to percentage points; K is a coefficient of conversion of methane flow reacting on said thermo-catalytic converting element to an electric signal being measured, [Bc/m 3 or Ac/m 3 ].