2 resultados para dibenzothiophene

em Aston University Research Archive


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The reactions of group 16 heterocycles with organometallic reagents are described. Thiophenes have been used as models for organic sulfur in coal and their reactivity towards triiron dodecacarbonyl has been investigated. Reaction of unsubstituted thiophene with Fe3(CO)12 results in desulfurisation of the heterocycle, with the organic fragment being recovered in the form of the ferrole, C4H4.Fe2(CO)6. In addition a novel organometallic compound of iron is isolated, the formula of which is shown to be C4H4.Fe3(CO)8. Bezothiophene reacts with Fe3(CO)12 to yield benzothiaferrole, C8H6S.Fe2(CO)6, in which the sulfur is retained in the heterocycle. Dibenzothiophene, a more accurate model for organic sulfur in coal, displays no reactivity towards the iron carbonyl, suggesting that the more condensed systems will desulfurise less readily. Microwave methodology has been successful in accelerating the reactions of thiophenes with Fe3(CO)12. However, reaction of benzothiophene does not proceed to the desulfurisation stage while dibenzothiophene is unreactive even under microwave conditions. Tellurophenes (Te analogues of thiophenes) are shown to mimic the behaviour of thiophenes towards certain organometallic reagents with the advantage that their greater reactivity enables recovery of products in higher yields. Hence, reaction of tellurophene with Fe3(CO)12 again affords the ferrole but with an almost ten-fold increase in yield over thiophene. More significantly, dibenzotellurophene is also detellurated by the iron carbonyl affording the previously inaccessible dibenzoferrole, C12H8.Fe2(CO)6, thereby demonstrating the mechanistic feasibility of dechalcogenation of the more condensed aromatic molecules. The potential of tellurium heterocycles to act as precursors for novel organometallics is also recognised owing to the relatively facile elimination of the heteroatom from these systems. Thus, 2-telluraindane reacts with Fe3(CO)12 to yield a novel organometallic compound of formula C16H16.Fe(CO)3, arising from the unsymmetric dimerisation of two organic fragments.

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A detailed study has been made of the feasibility of adsorptive purification of slack waxes from traces of aromatic compounds using type 13X molecular sieves to achieve 0.01% aromatics in the product. The limited literature relating to the adsorption of high molecular weight aromatic compounds by zeolites was reviewed. Equilibrium isotherms were determined for typical individual aromatic compounds. Lower molecular weight, or more compact, molecules were preferentially adsorbed and the number of molecules captured by one unit cell decreased with increasing molecular weight of the adsorbate. An increase in adsorption temperature resulted in a decrease in the adsorption value. The isosteric heat of adsorption of differnt types of aromatic compounds was determined from pairs of isotherms at 303 K to 343 K at specific coverages. The lowest heats of adsorption were for dodecylbenzene and phenanthrene. Kinetics of adsorption were studied for different aromatic compounds. The diffusivity decreased significantly when a long alkyl chain was attached to the benzene ring e.g. in dodecylbenzene; molecules with small cross-sectional diameter e.g. cumene were adsorbed most rapidly. The sorption rate increased with temperature. Apparent activation energies increased with increasing polarity. In a study of the dynamic adsorption of selected aromatic compounds from binary solutions in isooctane or n-alkanes, naphthalene exhibited the best dynamic properties followed by dibenzothiophene and finally dodecylbenzene. The dynamic adsorption of naphthalene from different n-alkane solvents increased with a decrease in solvent molecular weight. A tentative mathematical approach is proposed for the prediction of dynamic breakthrough curves from equilibrium isotherms and kinetic data. The dynamic properties of liquid phase adsorption of aromatics from slack waxes were studied at different temperatures and concentrations. The optimum operating temperature was 543 K. The best dynamic performance was achieved with feeds of low aromatic content. The studies with individual aromatic compounds demonstrated the affinity of type NaX molecular sieves to adsorb aromatics in the concentration range 3% - 5% . Wax purification by adsorption was considered promising and extension of the experimental programme was recommended.