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Carr's Compressibility Index Theory
Reports that the more a powder material compacts during a tapping test, the poorer its overall flow properties are.
Carr's Compressibility Index Equation
Calculated using the formula: C.I. = [(ρ_tapped - ρ_bulk) / ρ_tapped] * 100.
Excellent Flow Carr's Index
Indicated by a Carr's Compressibility Index strictly less than 10% (< 10%).
Good Flow Carr's Index
Indicated by a Carr's Compressibility Index ranging from 11% to 15%.
Fair Flow Carr's Index
Indicated by a Carr's Compressibility Index ranging from 16% to 20%.
Passable Flow Carr's Index
Indicated by a Carr's Compressibility Index ranging from 21% to 25%.
Poor Flow Carr's Index
Indicated by a Carr's Compressibility Index ranging from 26% to 31%.
Very Poor Flow Carr's Index
Indicated by a Carr's Compressibility Index ranging from 32% to 37%.
Very, Very Poor Flow Carr's Index
Indicated by an extremely high Carr's Compressibility Index exceeding 38% (> 38%).
Porosity (ε) Definition
A direct measure of the collective air spaces or voids present within a bulk bed of powder material.
Void Volume Formula (V_void)
Calculated mathematically as V_void = V_bulk - V_true.
Porosity Percentage Equation
Calculated mathematically as Porosity (ε) = (V_void / V_bulk) * 100.
Rhombohedral / Closest Packing
An extremely tight powder packing arrangement where angles of 60° and 120° dominate, resulting in a low porosity of 26%.
Cubic / Loosest Packing
An open powder packing arrangement where particles sit at 90° to one another, resulting in a high porosity of 47% to 48%.
Feret's Diameter (I)
The absolute distance between two imaginary parallel lines tangent to a randomly oriented particle and perpendicular to the ocular scale.
Martin's Diameter (II)
The diameter value calculated at the precise point that divides a randomly oriented particle into two equal projected surface areas.
Projected Area Diameter (III)
The diameter calculated from a theoretical perfect circle that possesses the exact same projected area as the asymmetrical particle.