Patent ID: 11958021
Assignee: ETAT FRANÇAIS REPRÉSENTÉ PAR LE DÉLÉGUÉ GÉNÉRAL POUR L'ARMEMENT
Field: Chemical engineering (Chemistry)
Classification: CPC B | IPC B

Claim 0:
1. A non-destructive method for determining the remaining filtration capacity of a given type of an adsorbent filter, the adsorbent filter being suitable for adsorbing a target gas, wherein the method comprises the following steps:
(a) selecting a first gas to be used as a probe and a second gas used as a carrier gas, both gases being able to pass, without remaining trapped, through the given type of adsorbent filter, unsaturated with target gas therein, the first gas having an adsorption isotherm such that at a partial pressure of 0.1 atmosphere of the first gas, the adsorption isotherm has an adsorption capacity of less than 100 μmol of first gas per gram of adsorbent, the first gas being intended for being mixed with the second gas, for injection into the given type adsorbent filter, the second gas having an adsorption isotherm such that, at a partial pressure of 0.1 atmospheres of second gas, the adsorption isotherm has an adsorption capacity of less than 100 μmol of second gas per gram of adsorbent,
(b) at a given operating temperature, pressure and hygrometry, selecting parameters for the injection of first gas and second gas into an adsorbent filter of the given type, the injection parameters comprising, for the first gas and the second gas, a given period and a flow-rate over time curve, the concentration of the first gas in the second gas including at least one abrupt variation during the injection period, each abrupt variation in the concentration of the first gas being characterized by an absolute value of the time derivative of the concentration of the first gas, which exceeds 100 ppmv/s,
for an adsorbent filter of the given type, called reference filter,
(c) injecting, at the given operating temperature, pressure and hygrometry, the first gas and the second gas into the reference filter according to the injection parameters of the step (b) and measuring, downstream of the reference filter, the evolution of the first gas concentration as a function of time for known increasing amounts of target gas adsorbed by the reference filter, the last amount corresponding to the breakthrough of the reference filter, and deducing the shut-off capacity ma of the reference filter as the mass concentration of target gas delivered during the injection time until the breakthrough multiplied by the flow rate through the filter multiplied by the time measured between the start of target gas injection at constant concentration and the time measured to reach the breakthrough concentration,
for an adsorbent filter of the given type for which the remaining filtration capacity is to be determined, called filter under test,
(d) injecting the first gas and the second gas into the filter, at the given operating temperature, pressure and hygrometry, the first gas and the second gas into the filter under test according to the injection parameters of the step (b) and measuring downstream of the filter under test, the evolution of the first gas concentration as a function of time;
(e) comparing the evolution of the first gas concentration as a function of time for the filter under test and for the reference filter, by mathematical analysis of the first gas concentration curve downstream of the filter as a function of the time to extract a signature from the curve representative of an abrupt variation upstream of the filter, the signature varying with the saturation rate of the filter, the signature extracted from the mathematical analysis of the first gas concentration curve downstream of the filter being one of:
the transition time from 95% to 5% of the maximum value of the first gas concentration downstream of the adsorbent filter obtained after the abrupt variation in first gas concentration;
the value of the first gas concentration peak measured downstream of the filter during the duration of the test;
the time period between the start of the abrupt variation of the first gas in the second gas flow and the quantifiable start of a change of concentration of first gas downstream of the filter;
one or a combination of parameters of a multi-parameter model of the first gas concentration curve measured downstream of the filter which, over the range of the saturation rate of the reference filter, has a monotonic variation and a maximum derivative depending on the saturation rate,
and then comparing the signature between the filter under test and the reference filter to a saturation rate value of the filter under test Tsft, and
(f) deducing the remaining filtration capacity of the filter under test by the following calculation: remaining filtration capacity=(1−Tsft)*Ma.