Performance of HZSM-5 agglomerated in a mesoporous matrix in the fuel production from ethylene at atmospheric pressure

Ethylene oligomerization into liquid fuels at slightly over atmospheric pressure has been studied due to its interest to valorize online the excess of ethylene in sustainable olefins production processes and to intensify the production of fuel from refinery secondary streams. Runs were carried out in a fixed-bed reactor under the following conditions: 1.5 bar; 275-375 degrees C; space time, 2.7-16.2 gcatalyst h molC  1; time on stream, 5 h. The catalyst was prepared by agglomerating a HZSM-5 zeolite (SiO2/Al2O3 of 30) in a mesoporous matrix (& gamma;-Al2O3/ & alpha;-Al2O3). The hierarchical porous structure of the catalyst enables to reach a pseudo-steady state with a remarkable remnant activity after an initial deactivation period of 2-3 h. Temperature shows a relevant effect on ethylene conversion and product distribution, where a C5+ liquid fuel yield of 55% above 325 degrees C and 10.6 gcatalyst h molC  1 is obtained. At 325 degrees C, gasoline yield is 60%, with high olefin content (49%), which decreases at higher temperature, due to an increase in aromatic and paraffin concentration. Soft and hard coke analysis reveal the role of the matrix to attenuate deactivation. Moreover, above 325 degrees C the cracking of hard coke precursors deposited in the zeolite micropores prevails respect to their formation.

Automated summary

The ethylene oligomerization into liquid fuels under slightly over atmospheric pressure is a promising way to utilize excess ethylene and intensify fuel production from refinery secondary streams. Experimental runs were conducted in a fixed-bed reactor using a hierarchical porous catalyst, and results showed a high yield of C5+ liquid fuel at temperatures above 325 degrees C. The matrix in the catalyst played a significant role in attenuating deactivation and the cracking of hard coke.