Carbon Footprint Analysis of Gasoline and Diesel from
Forest Residues and Algae using Integrated Hydropyrolysis and Hydroconversion
Plus Fischer–Tropsch (IH<sup>2</sup> Plus cool GTL)
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Abstract
Life cycle analysis
was conducted with a focus on greenhouse gas
(GHG) emissions of renewable gasoline and diesel produced by the integrated
hydropyrolysis and hydroconversion (IH<sup>2</sup>) and the new IH<sup>2</sup> plus Fischer–Tropsch (IH<sup>2</sup> Plus cool GTL)
processes. This new process has a primary objective of increasing
the yield of biofuel relative to original IH<sup>2</sup> process (increase
of 26% to 38% wt) by processing the C1–C3 gas co-products through
an integrated Fischer–Tropsch unit to produce liquid-range
hydrocarbon biofuel. For both biofuel processes, woody biomass residues
(forest logging and saw mills) and algae were investigated as feedstocks.
The effect of the electricity generation mix of different states in
the U.S. was also examined for algae cultivation. For woody residues
as feedstock, life cycle GHG emission savings of about 86.8% and 63.3%
were calculated for the IH<sup>2</sup> and optimized-IH<sup>2</sup> Plus cool GTL hydrocarbon biofuel, respectively, relative to fossil-derived
fuel. For algae as feedstock, emission increases of about 140% and
103% were calculated for the IH<sup>2</sup> and optimized-IH<sup>2</sup> Plus cool GTL, respectively, relative to fossil-derived fuel. The
electricity grid mix of the biorefinery location significantly impacts
the GHG emissions of the processes for algae feedstock. GHG savings
of about 42% can be potentially achieved if the plant was located
in an area with a low GHG intensity grid. This study has shown that
a significant biofuel yield boost can be achieved while retaining
high GHG savings by using IH<sup>2</sup> Plus cool GTL for a woody
feedstock