| Literature DB >> 21525995 |
Edward M Fisher1, Jessica L Williams, Ronald E Shaffer.
Abstract
Reusing filtering facepiece respirators (FFRs) has been suggested as a strategy to conserve available supplies for home and healthcare environments during an influenza pandemic. For reuse to be possible, used FFRs must be decontaminated before redonning to reduce the risk of virus transmission; however, there are no approved methods for FFR decontamination. An effective method must reduce the microbial threat, maintain the function of the FFR, and present no residual chemical hazard. The method should be readily available, inexpensive and easily implemented by healthcare workers and the general public. Many of the general decontamination protocols used in healthcare and home settings are unable to address all of the desired qualities of an efficient FFR decontamination protocol. The goal of this study is to evaluate the use of two commercially available steam bags, marketed to the public for disinfecting infant feeding equipment, for FFR decontamination. The FFRs were decontaminated with microwave generated steam following the manufacturers' instructions then evaluated for water absorption and filtration efficiency for up to three steam exposures. Water absorption of the FFR was found to be model specific as FFRs constructed with hydrophilic materials absorbed more water. The steam had little effect on FFR performance as filtration efficiency of the treated FFRs remained above 95%. The decontamination efficacy of the steam bag was assessed using bacteriophage MS2 as a surrogate for a pathogenic virus. The tested steam bags were found to be 99.9% effective for inactivating MS2 on FFRs; however, more research is required to determine the effectiveness against respiratory pathogens.Entities:
Mesh:
Substances:
Year: 2011 PMID: 21525995 PMCID: PMC3078131 DOI: 10.1371/journal.pone.0018585
Source DB: PubMed Journal: PLoS One ISSN: 1932-6203 Impact factor: 3.240
Phase 1 screening of FFRs for water absorbency and filtration efficiency.
| FFR Details | Water Content (g) | Filtration Efficiency (%) | ||||
| Model | Type | Contains Hydrophilic layer(s) | After decon. | 60 min | As received | After 1X |
| 3M 1870 | Surgical | no | 0.4 | 0.1 | 99.67 | 99.62 |
| 3M 1860 | Surgical | yes | 13.5 | 9.6 | 99.28 | 99.47 |
| KC PFR95 | Surgical | no | 0.9 | 0 | 96.13 | 95.77 |
| 3M 8210 | Particulate | yes | 11.6 | 8.2 | 99.88 | 99.34 |
| Cardinal Health | Particulate | yes | 12.8 | 11.2 | 99.62 | 99.56 |
| Moldex 2200 | Particulate | no | 1.5 | 0.2 | 98.52 | 99.24 |
*Data modified from references (10) and (14).
Determined using MSB X bags.
n = 1.
Phase 2 testing for water absorbency and filtration efficiency.
| FFR | Water Content (g) | Filtration Efficiency (%) | ||||
| Type | Model | After (3X) decon. | 30 min | As received | MSB X (3X) | MSB Y (3X) |
| Surgical | 3M 1870 | 1.7±1.4 | 0.1±0.1 | 99.7±0.1 | 98.6±0.6 | 99.0±1.1 |
| Surgical | KC PFR95 | 1.3±1.3 | 0±0 | 96.1±0.4 | 95.5±0.3 | 96.4±1.2 |
| Particulate | Moldex 2200 | 0.9±0.4 | 0.1±0.1 | 98.5±1.0 | 98.6±0.8 | 98.4±1.5 |
Determined using MSB X bags.
n = 3.
Decontamination efficacy of the microwave steam bags.
| FFR Model | MS2 from load controls | CV (%) | MS2 from Steam Treated FFR | Difference (Load vs. Treated) | Reduction (%) | |
|
|
| 7.57±0.08 | 18.5 | 4.47±0.32 | 3.10 | 99.90 |
|
| 7.09±0.17 | 37.6 | 3.85±0.35 | 3.25 | 99.93 | |
|
| 9.96±0.06 | 14.6 | 5.32±0.30 | 4.64 | 99.99 | |
|
|
| 6.93±0.16 | 32.8 | ≤3.69# | ≥3.24 | ≥99.94 |
|
| 8.15±0.25 | 62.3 | 4.70±0.69 | 3.45 | 99.93 | |
|
| 7.04±0.09 | 19.8 | ≤3.93# | ≥3.11 | ≥99.86 |
* Values in Log10 (pfu/FFR).
# Two of three trials reached detection limits.
Figure 1Photographs of the front (left) and back (right) panels of the microwave steam bags.
Top: MSB X bags. Bottom: MSB Y bags.
Figure 2Illustration of the components of the microwave steam bags and the placement of a typical FFR into the water reservoir.
Figure 3Schematic of the droplet loading method.