Biomedical Engineering Reference
In-Depth Information
TABLE 8.1
Comparison of the FAME Ester Content and Caloriic Value of the Biodiesel and Bio-oil from Microalgae
Method for
Extraction of Oil
HHV/Caloriic
Value
Microalgae
Process
Product
FAME Content
Ref.
Unidentiied
Using hexane as solvent
Transesteriication
Biodiesel
Not reported
40 MJ kg
−1
11
Chlorella vulgaris
(ESP 31)
Sonication to disrupt the cell wall
of microalgae and then vigorously
mixing the disrupted cell with
biphasic solvent of chloroform &
methanol
Transesteriication
Biodiesel
72.1% (from extracted
microalgal oil) 97.25%
(upon direct disruption of
algal biomass)
—
13
Chlorella sorokiniana
Two-step sequential hydrothermal
liquefaction
—
Bio-oil
—
40.8 MJ kg
−1
22
Sargassum patens
C. Agardh
Hydrothermal liquefaction
—
Bio-oil
—
27.1 MJ kg
−1
23
Spirulina
/HDPE
Co-liquefaction
—
Bio-oil
—
48.35 MJ kg
−1
24
Chlorella vulgaris
Microwave-assisted pyrolysis
—
Bio-oil
—
21.88 MJ kg
−1a
25
a
Low caloriic value reported that of microalgae
Chlorella vulgaris.
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