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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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1436 Aydin K. Sunol and Sermin G. Sunol<br />

Entrainer α Entrainer α<br />

Hexadecanol(1) - octadecane(2) - entrainer -<br />

ethane (120 bar, 70°C, y 0 = 15 wt%, a 0 = 2.5,<br />

y (1)+(2) = 30 wt%)<br />

methanol<br />

acetone<br />

hexane<br />

(120 bar, 90°C, y (1)+(2) = 20 wt%)<br />

methyl acetate<br />

benzene<br />

dichloromethane<br />

Separation factor, α =(y 2/x 2)/(y 1/x 2)<br />

2.2<br />

1.6<br />

1.6<br />

1.8<br />

1.2<br />

1.1<br />

Hexadecanol(1) - octadecane(2) - entrainer -<br />

carbon dioxide (120 bar, 70 °C, y 0 = 0.4 wt%,<br />

a 0 = 2.5, y (1)+(2) = 1 wt%)<br />

methanol<br />

acetone<br />

methyl acetate<br />

hexane<br />

Although entrainers provide the aforementioned added advantages, they also bring<br />

forth more complex process flowsheets. The separation <strong>of</strong> extract from entrainer and<br />

entrainer from the supercritical component are not as easy and as sharp as in the instances<br />

without entrainer. The selection <strong>of</strong> entrainer is based on thermodynamic, environmental,<br />

and economic considerations. The solute-entrainer and entrainer-supercritical separations<br />

are the key from the processing perspective. 52<br />

21.1.2.4 Reaction rate implication in supercritical solvents<br />

Reactions in supercritical media utilize high pressures. Therefore, the effect <strong>of</strong> pressure on<br />

reaction equilibrium as well as reaction rate plays an important role in supercritical phase<br />

reactions. 53<br />

The kinetics <strong>of</strong> the reaction can be explained in terms <strong>of</strong> the transition-state theory.<br />

According to the theory, the reaction occurs via a transition state species M* and the generic<br />

elementary reaction can be written as:<br />

aA + bB + ............ ↔ M* → Products<br />

The effect <strong>of</strong> pressure on the rate constant is given as:<br />

where:<br />

* *<br />

⎛∂lnk<br />

x ⎞ ∂lnK<br />

x ∂lnκ V<br />

⎜ ⎟ =<br />

⎝ ∂P<br />

⎠T<br />

∂P<br />

∂P<br />

T<br />

⎛ ⎞<br />

⎜ ⎟<br />

⎜ ⎟<br />

⎝ ⎠<br />

+⎛<br />

⎞<br />

⎜ ⎟ =<br />

⎝ ⎠<br />

Δ<br />

+<br />

RT P T<br />

⎛ ∂lnκ⎞ ⎜ ⎟<br />

⎝ ∂ ⎠<br />

T<br />

kx rate constant in mole fraction units<br />

P pressure<br />

T temperature<br />

K * x mole fraction based equilibrium constant for reaction involving reactants and transition<br />

state<br />

κT isothermal compressibility<br />

ΔV *<br />

activation volume (difference between partial molar volumes <strong>of</strong> activated complex and<br />

reactants), ΔV * =V * -aVA-bVB- ...<br />

R universal gas constant<br />

The rate constant in the above equation is expressed in terms <strong>of</strong> pressure independent<br />

units (mole fraction). If the rate constant is expressed in terms <strong>of</strong> pressure dependent units<br />

(such as concentration), the relevant equation is:<br />

3.4<br />

1.8<br />

1.6<br />

1.4

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