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Biodiesel Production from Spent Coffee GroundsAnthony Goh and Dr. Enrico N. Martinez School of Chemical Engineering, Purdue University, West Lafayette, IN USA 47906
AcknowledgementsSpecial thanks to:
• Katie Westfall, Port Café for supplying the spent coffee
grounds
• Dr. Bryan Boudoris for utilization of his laboratory space
and equipment
• Rohit Jaini for guidance on running GC-MS and data
interpretation
• Rick McGlothlin for assisting in the experimental setup
Did you
know?Coffee is the second most heavily traded
commodity only after petroleum and the largest food
import of the United States.
The global production number of coffee is
around 8 million tonnes per year with an increasing
demand every year. Thus, a sustainable coffee
industry requires the development of methods for
utilization of coffee byproducts.
This research project utilizes Soxhlet extraction method for the oil extraction process which then undergoes transesterification reaction to produce biodiesel. Preliminary results reveals that the maximum yield of coffee oil in spent coffee
grounds (SCG) is around 20 wt% and is dependent of the solvent used. Oil to biodiesel conversion is around 32.7 – 53.7% depending on the type of catalyst used and the operating conditions of the experiment.
0
10
20
30
40
50
60
1 2 3 4 5
37.1439.66
53.72 52.67
58.2
Perc
enta
ge (
%)
Sample Runs
Oil to Biodiesel Conversion
0
5
10
15
20
25
0 50 100 150 200 250 300
% Y
ield
Time (min)
Percentage Yield of Coffee Oil vs.
Time
0
5
10
15
20
25
1 2 3 4 5 6 7 8 9 10
% Y
ield
Sample Runs
Percentage Yield of Coffee Oil
Extracted
Hexane
Heptane
How?Future Directions• More repeated data to understand and produce the
reaction rate equation
• Analyze quality of biodiesel produced
• Analyze the system design and operating processes used
in industrial large scale production
References• L.S. Oliveira, A. S. Franca, R. R.S. Camargos, V. P.
Ferraz, Coffee oil as a potential feedstock for biodiesel
production, Biores. Technol., 99, 2008, 3244-3250.
• Z. Al-Hamamre, S. Foerster, Fr. Hartmann, M. Kröger, M.
Kaltschmitt, Oil extracted from spent coffee grounds as a
renewable source for fatty acid methyl ester
manufacturing, Fuel, 96, 2012, 70–76.
Conclusion• Operating temperature, type of solvent used for extraction
process, time affects the yield of coffee oil
• Immobilized enzyme catalyst L3170 is more effective than
soluble L4777 in oil to biodiesel conversion
• Max. yield of coffee oil from spent coffee grounds is around
20 wt% and is dependent on solvent used
• Oil to biodiesel conversion is around 32.7-53.7%
dependent on catalyst used and operating conditions
• GC-MS peaks detect presence of fatty acids palmitic,
linoleic, oleic and stearic
Sample
Run No.
Catalyst used
1 L4777 Repeated runs at fixed operating
conditions*2 L4777
3 L3170 Repeated runs at fixed operating
conditions*4 L3170
5 L3170 Increased temperature to 60C
Results
Transesterification – Catalyzed biochemical process
involving the conversion of a triglyceride (fat/oil) with
an alcohol to form esters and glycerol
Why?As the world’s fossil fuel reserves are depleting
rapidly, the demand for a more sustainable alternative
has risen. Alternatives that are scientifically
possible, environmentally acceptable and
technologically possible are being researched.
Biodiesel currently is known as one of the most
promising alternative energy source capable of
replacing fossil fuels in the future.
Solving two global concerns
• Reduction/Elimination of coffee waste
• Alternative to clean, cheap energy production
Separate and Recover
• Rotary evaporator
• Solvent recovery
(hexane/heptane)
• Immobilized enzyme can
be reused
React and Analyze• Transesterification
• Enzyme catalysis
• Immobilized (L3170)
• Soluble (L4777)
• Solution in reactor (methanol,
hexane, catalyst , coffee oil)
• Operating condition varied
• Analyzed using GC-MS
*Note: 140mL of methanol, 600 mL n-Hexane, 200 rpm stirrer speed, ~2g
of catalyst, 12g of coffee oil. Operating temperature at 50C
Extract and Filter• Soxhlet extractor via solvent
(heptane/hexane) extraction
method
• ~25g of SCG loaded into
cellulose thimble
• 600 mL of solvent/run
• Heated to sample’s B.P.
‘
Collect and Dry
• Placed in an isotemp
incubator operating at
70C
• Minimize/Eliminate
moisture content in
spent coffee grounds
(SCG)
Fatty Acid Chemical StructureConcentrations
(mM)
Weight
(%)
Palmitic
(C16:0)CH3(CH2)14COOH 6.678652 35.660
Stearic
(C18:0)CH3(CH2)16COOH 3.582774 19.130
Oleic
(C18:1)
CH3(CH2)7CH=CH(CH2)
7COOH0.926101 4.948
Linoleic
(C18:2)
CH3(CH2)3(CH2CH=CH)
2(CH2)7COOH1.003957 5.360
• Consistency in repeated data
• Higher coffee oil yield using hexane
• ~3 hours to reach max yield
• Higher biodiesel conversion using catalyst L3170
• Increasing T increases biodiesel conversion
Gas Chromatography Results