Abstract
A three-component kinetic model previously reported for uncatalyzed liquefaction has been used to simulate hydroliquefaction of Victorian brown coal with three different types of catalysts: iron-tin, iron, and haematite. The presence of catalyst is found to enhance hydrogenation of coal as well as the equilibrium hydrogenation-dehydrogenation reactions involving donor solvent. The thermal dissolution and autohydrogenation reaction rates are independent of catalyst used. Iron-tin-based catalyst has been found to be most effective for the hydrogenation reaction step. The simulation shows that the reactions producing hydrogen from tetralin are much slower than the coal-hydrogen reactions; hence, efforts aimed at efficient abstraction of hydrogen from the hydrogen donors may be beneficial.
| Original language | English |
|---|---|
| Pages (from-to) | 1825-1831 |
| Number of pages | 7 |
| Journal | Industrial & Engineering Chemistry Research |
| Volume | 26 |
| Issue number | 9 |
| DOIs | |
| Publication status | Published - 1 Sept 1987 |
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