Abstract
The selective separation of heavy n‐paraffins (C20–C30) from refinery slack wax was performed by adsorption onto zeolite molecular sieves (5A). Sorbents were characterized by thermogravimetric analyses, N2 adsorption, and mercury porosimetry. Three slack waxes: light, medium and heavy, were used, being analyzed by gas chromatography (GC) and simulated distillation. Several tests were carried out in a stirred batch reactor at high pressure and temperature for determining the system kinetics. Process variables were temperature (100–150°C), pressure (0.5, 1.5, and 2.5 MPa), and time (1–24 hr). Afterwards, adsorption isotherms in the range of 60–170°C were obtained for each wax by being fitted to a Langmuir type equation. Results showed that adsorption equilibrium is controlled by internal diffusion due to the large length of the normal paraffin chains, which have a diameter very close to the size of the zeolite channels. The amount of paraffin retained in the sieve is strongly influenced by the feedstock: lighter products adsorb more, also producing a higher purity n‐paraffin. The reverse trend is observed for the heavier feeds. However, adsorption of larger molecules (>n‐C32) is strongly hindered. For temperatures above 170°C, cracking reactions become more and more important.
Acknowledgment
The authors are indebted to Repsol Petróleo Research Center in Cartagena (Spain) for allowing the use of their laboratories and equipment.