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Original Articles

Optimizing Filtration Experiments for Length and Fractal Dimension Characterization of Non-Spherical Particles

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Pages 547-555 | Received 27 Jan 2015, Accepted 05 May 2015, Published online: 19 Jun 2015

Figures & data

FIG. 1. SEM image of the 1 μm pore diameter Nuclepore filter with 350 nm mobility diameter Ag agglomerates deposited.

FIG. 1. SEM image of the 1 μm pore diameter Nuclepore filter with 350 nm mobility diameter Ag agglomerates deposited.

FIG. 2. Comparison of Nuclepore filter penetrations among NaCl, soot agglomerates, and silver agglomerates at 5 cm s−1 face velocity. The zoom-in images of soot and silver agglomerates are also shown.

FIG. 2. Comparison of Nuclepore filter penetrations among NaCl, soot agglomerates, and silver agglomerates at 5 cm s−1 face velocity. The zoom-in images of soot and silver agglomerates are also shown.

FIG. 3. Penetration of Ag particles with different mass-mobility fractal dimensions. Manton model and Spurny-Kim model were in good agreement with data of Dfm = 3.0 and Dfm = 2.1, respectively. Penetrations for Ag particles with Dfm = 2.1, 2.2, 2.6, 2.9, and 3.0 are distinguishable.

FIG. 3. Penetration of Ag particles with different mass-mobility fractal dimensions. Manton model and Spurny-Kim model were in good agreement with data of Dfm = 3.0 and Dfm = 2.1, respectively. Penetrations for Ag particles with Dfm = 2.1, 2.2, 2.6, 2.9, and 3.0 are distinguishable.

FIG. 4. Comparison of experimental and theoretical penetrations at a lower face velocity of 2 cm s−1 for Ag particles with four different mass-mobility fractal dimensions. The model predicted the penetrations of three Ag particles with Dfm = 2.1, 2.3, and 3.0 very well.

FIG. 4. Comparison of experimental and theoretical penetrations at a lower face velocity of 2 cm s−1 for Ag particles with four different mass-mobility fractal dimensions. The model predicted the penetrations of three Ag particles with Dfm = 2.1, 2.3, and 3.0 very well.

FIG. 5. Relationship between the mobility diameter and effective length for Ag particles with different mass-mobility fractal dimensions.

FIG. 5. Relationship between the mobility diameter and effective length for Ag particles with different mass-mobility fractal dimensions.

FIG. 6. Mass-mobility fractal dimension as a function of penetration of fractal Ag particles with mobility diameters of 30–150 nm (left) and 180–400 nm (right).

FIG. 6. Mass-mobility fractal dimension as a function of penetration of fractal Ag particles with mobility diameters of 30–150 nm (left) and 180–400 nm (right).

FIG. 7. Effective length as a function of the penetration of fractal Ag particles.

FIG. 7. Effective length as a function of the penetration of fractal Ag particles.

FIG. 8. Comparison of experimental and theoretical penetrations for Ag particles with 2.1 and 3.0 Dfm through 3 μm pore diameter Nuclepore filters at 5 cm s−1 face velocity.

FIG. 8. Comparison of experimental and theoretical penetrations for Ag particles with 2.1 and 3.0 Dfm through 3 μm pore diameter Nuclepore filters at 5 cm s−1 face velocity.

FIG. 9. Suggested operational conditions for particles with mobility diameters of 50–100, 100–300, and 300–1000 nm by different pore diameter Nuclepore filters.

FIG. 9. Suggested operational conditions for particles with mobility diameters of 50–100, 100–300, and 300–1000 nm by different pore diameter Nuclepore filters.

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