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the production of thymoquinone from thymol and carvacrol

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is <strong>the</strong> simplest <strong>and</strong> most direct method. Pores are filled with a solution <strong>of</strong> metal salt <strong>of</strong><br />

sufficient concentration to give correct loading. Ion exchange is <strong>the</strong> reversible<br />

interchange <strong>of</strong> ions between a solid <strong>and</strong> a liquid. There is no permanent change in <strong>the</strong><br />

structure <strong>of</strong> <strong>the</strong> solid, which is <strong>the</strong> ion exchange material. Usually, contacting a zeolite<br />

with a salt solution <strong>of</strong> different cation performs ion exchange; one type <strong>of</strong> cation is<br />

replaced with o<strong>the</strong>r.<br />

The ion exchange process:<br />

zAB zB (z)+ zBA zA (s)+ zAB zB (s)+ zBA zA (z)<br />

Where zA <strong>and</strong> zB are <strong>the</strong> charges <strong>of</strong> <strong>the</strong> exchange cation A <strong>and</strong> B <strong>and</strong> <strong>the</strong> subscript z <strong>and</strong><br />

s refer to <strong>the</strong> zeolite <strong>and</strong> solution, respectively.<br />

A widely recognized modification <strong>of</strong> catalyst is to replace <strong>the</strong> Na + ions with<br />

o<strong>the</strong>r metal ions <strong>and</strong> <strong>the</strong>n reduce <strong>the</strong>m in situ so that <strong>the</strong> metal atoms are deposited<br />

within <strong>the</strong> framework. The resultant material displays <strong>the</strong> properties associated with a<br />

supported metal catalyst. Ion exchanged cation can induce new catalytic features in<br />

many reactions especially in liquid phase reactions, by <strong>the</strong>ir different size <strong>and</strong> chemical<br />

structure (Sheldon et al. 1998).<br />

2.5 Design <strong>of</strong> Stable Heterogeneous Catalysts<br />

Liquid phase oxidation is widely used in bulk chemical manufacture. It is<br />

becoming increasingly important in <strong>the</strong> syn<strong>the</strong>sis <strong>of</strong> fine chemical (Arends et al. 2001).<br />

Catalytic oxidations in <strong>the</strong> liquid phase generally employ soluble metal salts or<br />

complexes in combination with clean, inexpensive oxidants such as O2, H2O2, or RO2H.<br />

Heterogeneous catalysts are widely used in liquid phase oxidation reactions because <strong>of</strong><br />

<strong>the</strong>ir advantages.<br />

For heterogeneous catalysts; incorporation <strong>of</strong> <strong>the</strong> redox metal centre into <strong>the</strong><br />

surface <strong>of</strong> an oxide support is <strong>the</strong> conventional methods for <strong>the</strong> immobilizing metal<br />

catalyst. Such as heterogeneous Ti IV /SiO2 catalysts which is used for <strong>the</strong> epoxidation <strong>of</strong><br />

<strong>the</strong> propylene (Arends et al. 2001; Sheldon et al. 1998).<br />

Ano<strong>the</strong>r approach to design stable solid catalysts is confinement <strong>of</strong> redox metal<br />

ions or complexes into <strong>the</strong> framework or cavities <strong>of</strong> zeolites, redox molecular sieves.<br />

Unlike conventional supported catalysts; <strong>the</strong>y have a regular microenvironment with<br />

7

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