“…Sawdust was directionally converted into p ‐xylene by a one‐pot catalytic pyrolysis process under atmospheric pressure. The catalytic pyrolysis of sawdust for the production of aromatics was carried out in a fixed‐bed reactor using metal oxide‐modified HZSM‐5(80) catalysts, using the same procedures described in our previous work . Briefly, the system was mainly composed of a tube reactor, a feeder for solid reactants, two condensers and a gas analyzer.…”
Section: Methodsmentioning
confidence: 99%
“…The catalytic pyrolysis of sawdust for the production of aromatics was carried out in a fixed-bed reactor using metal oxide-modified HZSM-5(80) catalysts, using the same procedures described in our previous work. 32,33 Briefly, the system was mainly composed of a tube reactor, a feeder for solid reactants, two condensers and a gas analyzer. The ex-situ CFP of biomass was used in this work, including two cascade processes: pyrolysis of biomass and subsequent upgrading of biomass pyrolysis vapor in the two different zones of the reactor.…”
Section: Procedures For Production Of Biomass-based P-xylenementioning
“…Sawdust was directionally converted into p ‐xylene by a one‐pot catalytic pyrolysis process under atmospheric pressure. The catalytic pyrolysis of sawdust for the production of aromatics was carried out in a fixed‐bed reactor using metal oxide‐modified HZSM‐5(80) catalysts, using the same procedures described in our previous work . Briefly, the system was mainly composed of a tube reactor, a feeder for solid reactants, two condensers and a gas analyzer.…”
Section: Methodsmentioning
confidence: 99%
“…The catalytic pyrolysis of sawdust for the production of aromatics was carried out in a fixed-bed reactor using metal oxide-modified HZSM-5(80) catalysts, using the same procedures described in our previous work. 32,33 Briefly, the system was mainly composed of a tube reactor, a feeder for solid reactants, two condensers and a gas analyzer. The ex-situ CFP of biomass was used in this work, including two cascade processes: pyrolysis of biomass and subsequent upgrading of biomass pyrolysis vapor in the two different zones of the reactor.…”
Section: Procedures For Production Of Biomass-based P-xylenementioning
“…In previous studies, on the catalytic cracking of biomass and bio-oil [26,27], the catalysts of Ni/HZSM-5 and Re/Y were selected for the catalytic pyrolysis of lignin and for removing the functional groups of aromatics in the lignin-derived oil, respectively. HZSM-5 (25) zeolite with a Si/Al ratio of 25 obtained from Nankai University catalyst Co., Ltd. (Tianjin, China) was calcined in air atmosphere at 550 • C for 4 h prior to use.…”
The directional production of benzene is achieved by the current-enhanced catalytic conversion of lignin. The synergistic effect between catalyst and current promotes the depolymerization of lignin and the selective recombinant of the functional groups in the aromatic monomers. A high benzene yield of 175 g benzene /kg lignin was obtained with an excellent selectivity of 92.9 C-mol%. The process potentially provides a promising route for the production of basic petrochemical materials or high value-added chemicals using renewable biomass.
“…In our previous work, we have investigated using biomass or bio-oil for the production of aromatic chemicals, including C 6 -C 8 aromatics, ethylbenzene, cumene, phenol and C 8 -C 15 aromatics. [44][45][46][47][48] To produce bio-based PX, we also investigated recently the catalytic pyrolysis of sawdust over zeolites modified with single metal oxides such as La 2 O 3 , CeO 2 , MgO or ZnO. 42 The present work aimed to directionally convert furanic compounds into PX and understand the reaction mechanism.…”
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