Concluding remarks

During pyrolysis or liquefaction, biomass undergoes a series of complex conversion processes producing bio-oil. Bio-oils are highly diverse in its composition and has a spectrum of oxygenates. Due to the presence of a collective of different oxygenated compounds, an upgrading process to remove oxygen would likely involve a series of reactions. This review introduces several possibilities for upgrading bio-oil including dehydration, decarboxylation and decarbonylation. A summary of the best catalyst contenders for each reaction class is given in the Table 3.

Reaction class

Reaction details

Catalyst

Best performance

Dehydration

Methanolconversion to gasoline range products

HZSM-5,

ZnO/HZSM-5,

CuO/HZSM-5

CuO/HZSM-5 (7% loading of CuO is said to be best)

Ehtanol conversion to hydrocarbon

HZSM-5 ZnO/ ZSM-5 Ga2Os/ZSM-5 MozC/ ZSM-5 Re/ ZSM-5

GazO3/ZSM-5

Ehtanol to ethylene

dealuminated

modernite (DM)

Zn/DM

Mn/DM

Co/DM

Rh/DM

Ni/DM

Fe/ DM

Ag/DM

Zn on dealuminated modernite

Decarboxylation

Conversion of heptanoic acid to octane

Pd/SiOz

Ni/AlzOs

Pd/SiOz

Deoxygenation of stearic acid

5%Pd supported on messoporous silica — SBA15,

-MCM41

zeolyte-Y

5%Pd — SBA15

Ketonic condensation of acetic acid

MnOz, CeOz, MgO, ZnO, FezOs, KzO supported on SiO2, AlzOs, TiOz

CeOz supported on AlzO3, or on TiOz

Decarbonylation

Deoxygenation of methyl octanoate

Cs on NaX zeolyte

Cs on NaX zeolyte

Deoxygenation of acetaldehyde, acetone, butanone, and acetic acid

HZSM-5

HZSM-5

Table 3. Summary of best performing catalyst for each reaction class.

Hydrodeoxygenation has been the most frequently studied and one of the most reliable methods that could be used for deoxygenation of oxygenates. However, the drawbacks of hydrodeoxygenation include: the need for continuous replenishment of sulfur (for sulfided catalysts), and the non-selective deoxygenation of all bio-oil chemical moieties resulting in a spectrum of short-chained and long-chained hydrocarbons that are less useful as liquid fuels. The need of hydrogen makes resulting biofuels less competitive with existing petroleum fuels. More research is needed on development of effective non-sulfided hydrodeoxygenation catalysts. Preliminary investigations with Ni-Cu on CeO2 or ZrO2 may provide new directions on this front. Further research should be directed on identifying materials and processes will allay the need for using direct hydrogen.

According to the analysis, metal promoted or unpromoted HZSM-5 proves to be one of the most versatile catalysts that is capable of catalyzing all three deoxygenation reaction classes, i. e., dehydration, decarboxylation and decarbonylation. Nevertheless, the nanopore structure of HZSM-5 (~5.4-5.5 A), while assisting size selectivity for gasoline range hydrocarbons, also promotes pore blockages resulting in rapid catalyst deactivation. Developing catalysts of the same class, with larger and consistent pore structure and/or higher activity/functionality should be closely looked at.