“…Nelson et al have shown that RH values between 0% and 50% had no significant effect on the breakthrough time for 121 organic vapors, whereas above 60% RH, the dependence of the humidity became quite significant and was more important at lower concentrations [40]. These results are in agreement with another study that showed that water adsorption isotherm on activated carbon had increased sharply at about 50% RH [41]. But, contradicting results have been reported by Werner [42] who observed marked effect on breakthrough times below Table 3 Comparison of liquid adsorption capacities and ratio of the micropore volume occupied by an organic vapor at 24 L/min, 294 K, $ 500 ppm, and 40% RH per adsorbate-adsorbent systems.…”
Section: Micropore Characterization With Ovsupporting
confidence: 93%
“…The experimental pore volume values derived from the OV adsorption isotherm with different boiling points at the same concentration using the DR equation were within 0-19% for W OV-DRexp and 2-23% for W OV-DRcalc from the micropore volume derived from the Ar data. Thus reiterating the importance of having a specific structural constant which takes accounts the differences in the micropore structure [41]. With the exception of MSA Comfo, which has the widest pore size distribution and the largest specific surface area, in general, the micropore volume values obtained with OV adsorption isotherm were greater than those of Ar, especially for W OV-DRcalc .…”
Section: Comparison Of the Dr Prediction Approachesmentioning
confidence: 94%
“…For example, MIBK shows the greatest discrepancies (0.74-1.03 cm 3 OV/cm 3 Ar) and has the highest kinetic diameter of 7.35 Å (see Table 2) compared with DCM (0.13-0.18 cm 3 OV/cm 3 Ar), which has a small kinetic diameter of 3.3 Å comparable to that of CO 2 and Argon. Thus size exclusion effect is less pronounced for smaller molecules and may play a role in the adsorption of larger molecules for microporous activated carbon [41]. Moreover, the pore size distribution is another important contributor to the adsorption of OV onto activated carbon.…”
Section: Micropore Characterization With Ovmentioning
“…Nelson et al have shown that RH values between 0% and 50% had no significant effect on the breakthrough time for 121 organic vapors, whereas above 60% RH, the dependence of the humidity became quite significant and was more important at lower concentrations [40]. These results are in agreement with another study that showed that water adsorption isotherm on activated carbon had increased sharply at about 50% RH [41]. But, contradicting results have been reported by Werner [42] who observed marked effect on breakthrough times below Table 3 Comparison of liquid adsorption capacities and ratio of the micropore volume occupied by an organic vapor at 24 L/min, 294 K, $ 500 ppm, and 40% RH per adsorbate-adsorbent systems.…”
Section: Micropore Characterization With Ovsupporting
confidence: 93%
“…The experimental pore volume values derived from the OV adsorption isotherm with different boiling points at the same concentration using the DR equation were within 0-19% for W OV-DRexp and 2-23% for W OV-DRcalc from the micropore volume derived from the Ar data. Thus reiterating the importance of having a specific structural constant which takes accounts the differences in the micropore structure [41]. With the exception of MSA Comfo, which has the widest pore size distribution and the largest specific surface area, in general, the micropore volume values obtained with OV adsorption isotherm were greater than those of Ar, especially for W OV-DRcalc .…”
Section: Comparison Of the Dr Prediction Approachesmentioning
confidence: 94%
“…For example, MIBK shows the greatest discrepancies (0.74-1.03 cm 3 OV/cm 3 Ar) and has the highest kinetic diameter of 7.35 Å (see Table 2) compared with DCM (0.13-0.18 cm 3 OV/cm 3 Ar), which has a small kinetic diameter of 3.3 Å comparable to that of CO 2 and Argon. Thus size exclusion effect is less pronounced for smaller molecules and may play a role in the adsorption of larger molecules for microporous activated carbon [41]. Moreover, the pore size distribution is another important contributor to the adsorption of OV onto activated carbon.…”
Section: Micropore Characterization With Ovmentioning
“…35 The extent to which relative humidity affects the vapor phase adsorption process depends on the type of adsorbates, their partial pressures and the level of relative humidity. 6 Information related to the effect of water vapor on multicomponent vapor adsorption has been reported by Grant. 7 The wet adsorbate and wet adsorbent tests (RH = 80 percent) for two ternary mixtures of paraffins, aromatics and halocarbons were conducted in their study.…”
The effects of water vapor on binary vapor adsorption of toluene and methylene chloride by activated carbon were investigated on a bench-scale experimental system. Three levels of relative humidity (15,65 and 90 percent) in conjunction with different concentrations of individual adsorbates (from 400 to 1200 ppmv) were tested by tracing the breakthrough curves of each adsorbate eluted from a fixed-bed adsorber. The adsorption capacities of the activated carbon tested for each adsorbate under the various conditions were obtained from calculations based on area integration of the breakthrough curves. It was found that with increasing relative humidity, the shape of breakthrough curves was asymmetrically distorted and the width of the breakthrough curves was broadened for toluene and steepened for methylene chloride. The adsorption capacities for both toluene and methylene chloride were decreased with the increase of relative humidity. The magnitude of the effect of water vapor is greater at the lower toluene concentration and at the higher concentration of methylene chloride. The mechanisms of water vapor influence on the process of multicomponent vapor adsorption are discussed.
“…The flow rate of 24 l/ min through the OV cartridge was chosen as the equivalent breathing rate for moderate work. The breakthrough tests were performed at 40% RH and the adsorption of water vapor at this RH is considered insignificant Werner et al, 1986). A concentration of 500 ppm was chosen as a reasonable amount to achieve 100% saturation in a controllable time manner for all the tested vapors.…”
Section: Miniaturized (Mini) and Ov Cartridgesmentioning
Breakthrough experiments are essential for the characterization of the adsorption capacity and micropore volume of activated carbon respiratory cartridges and for the validation and determination of cartridge service life models. In an effort to gain better control over environmental conditions in breakthrough tests and to obtain reliable data, a novel experimental approach using a miniaturized (Mini) cartridge was designed to replicate a small section of a respiratory cartridge. The Mini device and the organic vapor respiratory cartridge were tested in single and parallel experiments where in the former, one filter was tested one at a time and in the latter both devices were exposed simultaneously to the same conditions. The Mini device gave comparable results to the 10% breakthrough times and adsorption capacities of the organic vapor cartridges. The reproducibility of the packed carbon bed of the Mini provided strong support for using the Mini in breakthrough experiments for the characterization of the activated carbon adsorption capacity and estimation of cartridge service life.
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