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Thomas T. Mercer's Aerosol Technology in Hazard Evaluation PDF

By Thomas T. Mercer

ISBN-10: 0124911501

ISBN-13: 9780124911505

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Additional info for Aerosol Technology in Hazard Evaluation

Example text

5 THE KINETIC REACTION When air velocity changes, either in magnitude or in direction, particles suspended in it will lag behind owing to their inertia, giving rise to the kinetic reaction, — mdU/dt, where U is the relative velocity between air and particle. 27) so that their velocity relative to the air diminishes exponentially: U = U0exp(-t/mZ). 28) Conversely, a particle injected into still air at the initial velocity U0 is slowed down according to the same equation. The distance S0 that the particle will Properties Affecting Aerosol Stability 2-2 41 travel before coming to rest is of considerable interest and can be found readily by dividing both sides of Eq.

Courtesy of Academic Press, New York. 5 THE KINETIC REACTION When air velocity changes, either in magnitude or in direction, particles suspended in it will lag behind owing to their inertia, giving rise to the kinetic reaction, — mdU/dt, where U is the relative velocity between air and particle. 27) so that their velocity relative to the air diminishes exponentially: U = U0exp(-t/mZ). 28) Conversely, a particle injected into still air at the initial velocity U0 is slowed down according to the same equation.

Properties Affecting Aerosol Stability 2-2 47 dCJdt = - 3 . 38a) and dCJdt = - 3 . 0 x 10-Vp/VC m exp(21n 2 a g )/// = - £/G3Cmexp(2 In2 ag)/H. 38b) D3 and σ8 are, respectively, the mass median diameter in micrometers and the geometric standard deviation of the initial size distribution. UG3 is the terminal settling velocity in centimeters per second corresponding to D3. Both stirred settling [45] and tranquil settling [44] have been used to estimate size distribution parameters. (b) Coagulation.

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Aerosol Technology in Hazard Evaluation by Thomas T. Mercer


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