Table 41. Aromatics Yields for Catalytic Co-pyrolysis of Pure Glycerol with Various Co-feeds.

Entry	Co-feeds	Catalyst	Conditions	Result	Ref
1	Glycerol and H2O	15%CNT-OH/H-ZSM-5/Sono	Continuous fixed-bed reactor, glycerol/H2O 40/60 wt%, T: 400 °C, P: 1 atm, N2, and WHSV: 0.71 h–1	BTX peak carbon yield of 27.4 C%; catalyst lifetime of ca. 8.5 h	(1076)
2	Glycerol and alcohols	20Zn@Sn/H-ZSM-5	Continuous fixed-bed reactor, glycerol/CH3OH 40/60 wt%, T: 400 °C, P: 1 atm, N2, and WHSV: 0.71 h–1	BTX peak carbon yield of 38 C%; catalyst lifetime of ca. 10.5 h	(1077)
3	Glycerol and alkanes	Pd1.1-Zn9.2/Y2O3-Al2O3 extruded with H-ZSM-5 and bentonite	Continuous fixed-bed reactor, glycerol/hexane 50/50 wt%, T: 635 °C, P: 1 atm, steam, and WHSV: 1.5 h–1	BTX mass yield of 12.0 wt%	(1078)
4	Glycerol and vegetable oil	H-ZSM-5/Al2O3 (60/40 wt%)	Continuous fixed-bed reactor, glycerol/oleic acid 45/55 wt%, T: 550 °C, N2, P: 1 atm, and WHSV: 1 h–1	Peak BTX yield of 26.7 C%; BTX productivity of 834 mgBTX g–1catalyst during a catalyst lifetime of ca. 11 h	(1079)