Homogeneous and Heterogeneous Catalysis Impact on Pyrolyzed Cellulose to Produce Bio-Oil

Catalytic upgrading of penicillin fermentation residue bio-oil by metal-supported HZSM-5

Antibiotic fermentation residue (AR) is composed of hazardous organic waste produced by the pharmaceutical industry. AR can be effectively converted into bio-oil by fast pyrolysis, but its high nitrogen content limits the prospect of bio-oil as a fuel resource. In order to further reduce the nitrogen content of AR bio-oil, we have examined the catalytic removal of N and O from penicillin fermentation residue (PR) bio-oil under fast pyrolysis conditions. We have used M/HZSM-5 (M = Fe, Co, Ni, Cu, Zn, Zr, Mo, Ag and Ce) metal catalysts, with a metal oxide content of 10%. Additionally, the effect of mixed and separated catalytic forms on catalytic upgrading were analyzed, and changes in the catalyst itself before and after pyrolysis under separated catalytic conditions were specifically investigated. Our results show that the metal elements in the fresh catalyst will exist in the form of oxides, ions and simple metals. In-situ reduction caused by pyrolysis gas in the catalytic pyrolysis process makes some ionic metals (e.g., Co²⁺, Cu²⁺ and Ag⁺) in the catalyst transform into oxides, and some metal oxides are reduced to simple metals or suboxides (including Fe, Ni, Cu and Mo). The N content in the mixed catalytic bio-oil decreased from 10.09 wt% to Zn/HZSM-5 (6.98 wt%), Co/HZSM-5 (7.1 wt%), Cu/HZSM-5 (7.18 wt%) and Ce/HZSM-5 (7.18 wt%). We also observed significant reduction in the O content (9.77 wt%) with Ag/HZSM-5 (3.75 wt%), Mo/HZSM-5 (6.86 wt%), Ce/HZSM-5 (8.39 wt%) and Fe/HZSM-5 (8.54 wt%) in the separated catalytic bio-oil. The Ni/HZSM-5 catalystcan reduce the organic acid content in bio-oil from 22.9% to 10.8%. The separated catalysis methodology also promoted an increase of hydrocarbons in the bio-oil: Zn/HZSM-5, Ag/HZSM-5, Mo/HZSM-5, Zr/HZSM-5 and Ce/HZSM-5 reached 11.6%, 11.5%, 11.1%, 10.1%, and 8.8%, respectively. Carbon deposition formed by aromatic carbon/graphite carbon, pyrrole and pyridine compounds leads to deactivation of the catalyst.

Recyclabl Metal (Ni, Fe) Cluster Designed Catalyst for Cellulose Pyrolysis to Upgrade Bio-Oil

A new recyclable catalyst for pyrolysis has been developed by combining calculations and experimental methods. In order to understand the properties of the new cluster designed catalysts, cellulose (a major component of plants) as a biomass model compound was pyrolyzed and catalyzed with different cluster designed catalysts. The NiaFeb (2 ≤ a + b ≤ 6) catalyst clusters structures were calculated by using Gaussian and Materials Studio software to determine the relationships between catalyst structure and bio-oil components, which is essential to design cluster designed catalysts that can improve bio-oil quality. GC-MS analysis of the bio-oil was used to measure the effects on the different catalyst interactions with cellulose. It was found that the NiFe cluster designed catalysts can increase the yield of bio-oil from 35.8% ± 0.9% to 41.1% ± 0.6% and change the bio-oil composition without substantially increasing the water content, while substantially decreasing the sugar concentration from 40.1% ± 1.3% to 27.5% ± 0.9% and also producing a small amount of hydrocarbon compounds. The catalyst with a high Ni ratio also had high Gibbs free energy, ΔG, likely also influencing the decrease of sugar and acid while increasing the ketone concentrations. These results indicate the theoretical calculations can enhance the design next-generation cluster designed catalysts to improve bio-oil composition based upon experiments.

Catalytic Fast Pyrolysis of Biomass into Aromatic Hydrocarbons over Mo-Modified ZSM-5 Catalysts

Mo-modified ZSM-5 catalysts were prepared and used to produce aromatic hydrocarbons during catalytic fast pyrolysis (CFP) of biomass. The composition and distribution of aromatics were investigated on pyrolysis–gas chromatography/mass spectrometry (Py-GC/MS). The reaction factors, such as the Mo content, the reaction temperature and the catalyst/biomass mass ratio, were also optimized. It was found that the 10Mo/ZSM-5 catalyst displayed the best activity in improving the production of monocyclic aromatic hydrocarbons (MAHs) and decreasing the yield of polycyclic aromatic hydrocarbons (PAHs) at 600 °C and with a catalyst/biomass ratio of 10. Furthermore, according to catalyst characterization and the experiment results, the aromatics formation mechanism over Mo/ZSM-5 catalysts was also summarized and proposed.