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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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1432 Aydin K. Sunol and Sermin G. Sunol<br />

Most <strong>of</strong> the theoretically based estimation methods for viscosity <strong>of</strong> dense gases rely on<br />

modified Enskog theory. Corresponding states based methods are also popular but should<br />

be used with care due to their empiric nature.<br />

21.1.2.2.2 Diffusivity<br />

The experimental techniques used to measure the diffusion are based upon chromatographic<br />

methods, 19 NMR (for self-diffusion), and photon correlation spectroscopy. 45<br />

The so called chromatographic method for the measurement <strong>of</strong> diffusion coefficients,<br />

strictly speaking, is not a chromatographic method since no adsorption/desorption or retention<br />

due to partition in two phases are involved in the method. The experimental system<br />

used is however a chromatograph. Diffusion occurs in an empty, inert column on which the<br />

fluid phase is not supposed to be adsorbed. The fluid, in which the solute diffuses flows,<br />

continuously through the empty column and the solute, which is introduced into the column<br />

at one end, is detected at the other end as effluent concentration.<br />

The theory <strong>of</strong> diffusion in flowing fluids is first given by Taylor 46 and Aris. 47 According<br />

to Aris, a sharp band <strong>of</strong> solute, which is allowed to dissolve in a solvent flowing<br />

laminarly in an empty tube, can be described in the limit <strong>of</strong> a long column as a Gaussian distribution,<br />

the variance <strong>of</strong> which, σ 2 , in length units is:<br />

where:<br />

()<br />

2<br />

σx = 2D<br />

t<br />

eff<br />

t time <strong>of</strong> migration <strong>of</strong> the peak<br />

Deff effective diffusion coefficient given by,<br />

r u<br />

Deff = D12<br />

+<br />

48D<br />

2 2<br />

12<br />

where:<br />

u average solvent velocity<br />

r inner radius <strong>of</strong> the tube<br />

D12 binary diffusion coefficient.<br />

The first term describes the longitudinal diffusion in the axial direction. The second<br />

term is called the Taylor diffusion coefficient and describes band broadening due to the parabolic<br />

flow pr<strong>of</strong>ile and therefore radial diffusion. The height equivalent to a theoretical<br />

plate, H, is a measure <strong>of</strong> the relative peak broadening and is defined as<br />

()<br />

2<br />

H =σ x / L<br />

where:<br />

L length <strong>of</strong> the tubing.<br />

Combining the above equations yields<br />

2 2D12<br />

r u<br />

H = +<br />

u 24D<br />

12<br />

Bulk diffusivity can be calculated from the above equation.

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