1. System Preparation
2. Material Preparation
3. Aerosolization
4. Characterization
5. Post-sampling Operations and Clean-up
Figure 2 shows a typical example of total aerosol particle number concentration and size changes over time, using the above protocols in an aerosolization experiment with hydrophobic SiO2. Particle concentrations started to rise as soon as the aerosolization flow was introduced. The geometric mean size of particles gradually increased as well. After approximately 10 SMPS scans (3.5 min/scan), the aerosol started to enter a steady state, where particle concentration and mean diameter no longer varied by any significant amount. This state lasted more than 30 min, which was sufficient to complete ten 3-min SMPS scans. Figure 3 shows the change in particle concentration in the form of individual size distributions (based on the same data as in Figure 2). The peak rose slowly over time, and once the aerosol became stable, it remained within the same size range throughout the rest of the test.
The very small mean diameter shown at the beginning of the experiment was not due to unstable powder aerosolization. Rather, it was caused by the residual ambient air inside the funnel after the powder filling procedure. This volume of air was the first to flow into the measurement chamber and was sampled by the SMPS during its initial scans (Figure 4). This could be avoided by carrying out all the experiments in a clean room if this was required by the scientific question at hand. Indeed, the size distribution of the first scan was very similar to that of the ambient air. As the powder aerosol particles continued to flow in, the interference from the ambient particles diminished rapidly, and the effect had nearly disappeared after a few SMPS scans.
Figure 2. Change in total particle number concentration and mean diameter in an aerosolization experiment (241 mg hydrophobic SiO2; aerosolization flow 0.3 L/min). Please click here to view a larger version of this figure.
Figure 3. Change in particle size distribution in an aerosolization experiment. Please click here to view a larger version of this figure.
Figure 4. Aerosol particle size distributions at the beginning of the aerosolization test. Particle concentration is presented on a relative scale (normalized to the total number) in order to compare the spectrum from the first scan in a very low concentration to spectra from later scans in higher concentrations. Please click here to view a larger version of this figure.
The changes in particle concentration do not always follow the same patterns. Four possibilities can usually be seen in an aerosolization test. In Figure 5A, the concentration slowly increased to a "plateau" region, then remained nearly unchanged for the rest of the experiment. In Figure 5B, the concentration first rose to a maximum point, gradually decreased to a low level, and then remained stable for more than 1.5 hr. In Figure 5C, the concentration continued decreasing to zero. In Figure 5D, the concentration increased to a maximum level, remained there for a certain period, and then decreased again.
Scenario (a) is usually seen when the standard operating procedure is followed. The aerosolization air flow is slowly introduced and finally stabilized within the proper range. The amount of raw material is sufficient with respect to the aerosolization level, and a constant aerosol generation rate can be maintained for a long period of time. Scenario (b) is most likely due to an excessive aerosolization flow throughout the experiment, combined with an insufficient quantity of powder. The powder is rapidly consumed and is not able to sustain stable aerosol generation. Scenario (c) shows a similar drop in particle number concentration to Scenario (b) except that after a short time, the air flow rate was re-adjusted to a suitable range and kept constant throughout the rest of the test. This allowed the particle concentration to gradually reach a stable range. Scenario (d) appears when an insufficient amount of raw material is used. At the latter phase of the experiment, there is no longer enough test powder to generate aerosol particles at a constant rate, as was possible in the early phase of aerosolization. Consequently, the particle concentration in the system decreases.
Figure 5. Typical patterns for changing total particle concentrations during aerosolization experiments: (A) slowly increase until a plateau is reached; (B) gradually decrease to zero; (C) rapidly reach a peak and then decrease to a stable level; (D) increase to a steady state and maintain for a certain period of time, then decrease. Please click here to view a larger version of this figure.
Different aerosolization flow rates were tested in order to study their influence on aerosol generation. Flow rates from 0.3-1.1 L/min were used, and the resulting particle size distributions are shown in Figure 6. The peak of the spectrum rose as the flow increased. At the highest flow rate (1.1 L/min), micron-sized airborne particles started to enter the system (the secondary peak). The modal sizes of the aerosol particles stayed similar when under the same aerosolization flow, however, they decreased gradually when air flow increased through the range from 0.3-0.7 L/min (Figure 7). The increasing particle generation rate and diminishing mean particle diameter as flow rates increased suggest that the more dynamic aerosolization process (with significant particle movements and collisions) facilitated deagglomeration of powder particles, resulting in a modified size distribution of the aerosol particles generated.
Figure 6. Changing particle size distributions with increasing air flow rates (0.3-1.1 L/min). Please click here to view a larger version of this figure.
Figure 7. Comparison of particle size distributions under different flow rates. The spectra were turned into similar heights in relative scale (normalized to total particle number), which shows better the shift of the peak. Please click here to view a larger version of this figure.
The particle number concentrations of aerosols generated in replicate tests can vary by up to several folds, but usually well within one order of magnitude. The mean particle size, on the other hand, is highly reproducible. Figure 8 shows an example of the variation in particle size distribution from four replicate tests using the same material. The standard deviation was 39.7% for the total particle concentration and 6.6% for the geometric mean size. The variation of the number concentration could be due to several reasons: 1) different raw material status (e.g., agglomeration level); 2) human factors in powder filling process (influence the powder quantity deposited at the funnel bottom, thus the amount available for aerosolization); or 3) air flow adjustment at the beginning of aerosolization.
Figure 8. Variation of test results from replicate aerosolization experiments with hydrophobic SiO2. The error bars represent the standard deviation of particle number concentration in individual size channels. Please click here to view a larger version of this figure.
titanium dioxide nanopowder | JRC | NM-103/104 | Reference materials provided within EU FP7 MARINA project |
silicon dioxide nanopowder | AEROSIL | R974 | |
silicon dioxide nanopowder | JRC | NM-200 | Reference materials provided within EU FP7 MARINA project |
zinc oxide nanopowder | JRC | NM-110/111 | Reference materials provided within EU FP7 MARINA project |
cerium dioxide nanopowder | JRC | NM-211/212 | Reference materials provided within EU FP7 MARINA project |
The V-shaped aerosol generator | Souffleur de verre S.A. | Specially made based on conditions required in the experiments (e.g., geometry, thickness) | |
scanning mobility particler sizer (SMPS) | GRIMM | Model N° 5.403 | Size range: 11.1–1083.3 nm (impactor: d50=1082 nm); composed of a condensation particle counter (CPC) and a dynamic mobility analyzer (DMA); sampling flow ate: 0.3 L/min; sheath flow rate: 3.0 L/min; with standard multiple charge correction and diffusion loss correction; |
optical particle counter (OPC) | GRIMM | Model N° 5.403 | Size range: 0.25-32 µm |
mini-particle sampler (MPS) | ECOMESURE | ||
transport tubes | Milian S.A. | 8 mm-conductive | 6 mm inner diameter |
Nanoparticle aerosols released from nanopowders in workplaces are associated with human exposure and health risks. We developed a novel system, requiring minimal amounts of test materials (min. 200 mg), for studying powder aerosolization behavior and aerosol properties. The aerosolization procedure follows the concept of the fluidized-bed process, but occurs in the modified volume of a V-shaped aerosol generator. The airborne particle number concentration is adjustable by controlling the air flow rate. The system supplied stable aerosol generation rates and particle size distributions over long periods (0.5-2 hr and possibly longer), which are important, for example, to study aerosol behavior, but also for toxicological studies. Strict adherence to the operating procedures during the aerosolization experiments ensures the generation of reproducible test results. The critical steps in the standard protocol are the preparation of the material and setup, and the aerosolization operations themselves. The system can be used for experiments requiring stable aerosol concentrations and may also be an alternative method for testing dustiness. The controlled aerosolization made possible with this setup occurs using energy inputs (may be characterized by aerosolization air velocity) that are within the ranges commonly found in occupational environments where nanomaterial powders are handled. This setup and its operating protocol are thus helpful for human exposure and risk assessment.
Nanoparticle aerosols released from nanopowders in workplaces are associated with human exposure and health risks. We developed a novel system, requiring minimal amounts of test materials (min. 200 mg), for studying powder aerosolization behavior and aerosol properties. The aerosolization procedure follows the concept of the fluidized-bed process, but occurs in the modified volume of a V-shaped aerosol generator. The airborne particle number concentration is adjustable by controlling the air flow rate. The system supplied stable aerosol generation rates and particle size distributions over long periods (0.5-2 hr and possibly longer), which are important, for example, to study aerosol behavior, but also for toxicological studies. Strict adherence to the operating procedures during the aerosolization experiments ensures the generation of reproducible test results. The critical steps in the standard protocol are the preparation of the material and setup, and the aerosolization operations themselves. The system can be used for experiments requiring stable aerosol concentrations and may also be an alternative method for testing dustiness. The controlled aerosolization made possible with this setup occurs using energy inputs (may be characterized by aerosolization air velocity) that are within the ranges commonly found in occupational environments where nanomaterial powders are handled. This setup and its operating protocol are thus helpful for human exposure and risk assessment.
Nanoparticle aerosols released from nanopowders in workplaces are associated with human exposure and health risks. We developed a novel system, requiring minimal amounts of test materials (min. 200 mg), for studying powder aerosolization behavior and aerosol properties. The aerosolization procedure follows the concept of the fluidized-bed process, but occurs in the modified volume of a V-shaped aerosol generator. The airborne particle number concentration is adjustable by controlling the air flow rate. The system supplied stable aerosol generation rates and particle size distributions over long periods (0.5-2 hr and possibly longer), which are important, for example, to study aerosol behavior, but also for toxicological studies. Strict adherence to the operating procedures during the aerosolization experiments ensures the generation of reproducible test results. The critical steps in the standard protocol are the preparation of the material and setup, and the aerosolization operations themselves. The system can be used for experiments requiring stable aerosol concentrations and may also be an alternative method for testing dustiness. The controlled aerosolization made possible with this setup occurs using energy inputs (may be characterized by aerosolization air velocity) that are within the ranges commonly found in occupational environments where nanomaterial powders are handled. This setup and its operating protocol are thus helpful for human exposure and risk assessment.