Biofuel Production From Biodegradable Resources

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Biofuel Production from biodegradable resources
Biofuel type

Specific name

Biodiesel

-

-

Biodiesel
from energy
crops: methyl
and ethyl
esters of fatty
acids
Biodiesel
from waste

Feedstock
-

-

Oil crops (e.g. rapeseed, oil
palm, soy, canola, jatropha,
castor, …)
Waste cooking/frying oil &
other biomass/waste
biomass

Conversion
Technologies
-

-

Cold and
w a rm
pressing
extraction,
transesterific
ation ,
esterification
(may include
hydrolysis as
a preprocessing
step)

Bioethanol

Biogas

Pyrolytic biooil

Conventional bioethanol

Sugar beet, sugar cane, grain

Biogas/CH

organic waste

Bio-oil/ pyro-oil

lignocellulosic biomass

4

fermentation

Acid
fermentation
and
methane
formation
pyrolysis

Typical Biomass Pyrolysis Products

Fast Pyrolysis of Biomass:


Fast pyrolysis is a thermal process that rapidly heats biomass to a carefully controlled temperature
(~500°C), then very quickly cools the volatile products (<2 sec) formed in the reactor


Offers the unique advantage of giving a liquid that can be stored and transported.



Has been developed in many configurations

Typical characteristics of Bio-oil (pyro-oil):
Water miscible and is comprised of many oxygenated organic chemicals.


Combustible,



Not miscible with hydrocarbons,



Heating value ~ 17 MJ/kg,



Density ~ 1.2 kg/l,



Acid, pH ~ 2.5,

Some demerits of pyro-oil: Pungent odor, water miscibility, “Ages” - viscosity increases with time, much
lower CV(heating value) compared to biodiesel/other petroleum fuels, Acid, pH ~ 2.5.
Blending with alcohol/additives may improve certain properties.

BIODIESEL
Environmental and Energy Issues
• Combustion of fossil fuels increases atmospheric levels
of carbon dioxide/GHG emission/global warming
• Fossil fuels are finite resources

Advantages of Biodiesel:
Renewable, eco-friendly & Sustainable source of
energy
Foreign Exchange Savings
Can be blended in any ratio with petroleum
diesel.
Can be used in existing diesel engines without
modification.
Similar calorific value as petroleum diesel.
Also eliminates the huge cost of revamping the
nationwide fuel distribution infrastructure.
Environmental Benefits
 Reduction in GHG Emission/ Global warming
 Effective solid and liquid waste management

Biodiesel, a fuel, which consists of mono-alkylester(s) of long chain fatty acid(s) derived from
vegetable oils or animal fat(s) designated B100.
Oils & Fats of Plant And Animal Origins Are the
major Feed Stocks
1. Refined vegetable Oils
2. Acidic Oils/fats of Low or High FFA(free fatty
acids)
(i)Virgin Oils (Soybean, Rice bran, Mustard,
palm)
(ii)Used Frying Oils/waste cooking Oils.
(iii) Animal fats with high FFA

Homogeneous Base Catalyzed Conversions
Base catalyzed processes dominate current
commercial production : Sensitive to water and free
fatty acids;Typical alcohol to oil ratio varies
between 6:1 and 10:1 (mole ratio);Typical catalyst
concentrations (w/w, %)
NaOH/KOH

0.3-1.4%

Na-Methoxide

0.5% or less

Homogeneous Acid Catalyzed Conversions
 Direct esterification, oils with high free fatty acid
content
 Requires water removal
 Requires high alcohol: free fatty acid ratio, i.e. 40:1
 Requires large amount of catalyst (5-25%)

Heterogeneous Catalytic Process Highlights

 Batch/Continuous technology based on solid
catalyst
 High glycerol purity >98%
 Very high ester yield: close to 100%
 No waste production of low-value fatty acids
 No waste saline streams that require disposal
 Much lower catalyst requirements (per ton of
FAME) compared with other processes, as the
heterogeneous catalysts are reusable.

Biodiesel Specifications
Fuel Property

Method

Limits

Units

ASTM
Flash point, closed cup

D 93

130 min

°C

Water and sediment

D 2709

0.050 max

% volume

Kinematic viscosity, 40 ° C

D 445

1.9 – 6.0

Sulfated ash

D 874

0.020 max

wt. %

Total Sulfur

D 5453

0.05 max

wt. %

Copper strip corrosion

D 130

No. 3 max

Cetane number

D 613

47 min

Cloud point

D 2500

Report to customer

°C

Carbon residue

D 4530

0.050 max

wt. %

Acid number

D 664

0.80 max

mg KOH/g

Free glycerin

D 6584

0.020

wt. %

Total glycerin

D 6584

0.240

wt. %

Phosphorus

D 4951

0.0010

wt. %

Vacuum distillation end point

D 1160

360 max

°C

2

mm /s

Conclusion:
1. Waste cooking oil/ animal fat/vegetable oil(s) can be
potential feedstock(s) for production of Biodiesel
2. Highly efficient, cost-effective, reusable
heterogeneous (acid/base/ bi-functional) catalyst(s) can
be prepared from solid municipal and industrial wastes
which can be applied to produce fuel grade biodiesel
from various grades of oil/fat (waste/virgin/mixed)
3. Waste valorization and eco-friendly operation,
paving the path to a greener and cleaner world .

Note: For further study, read paper
no.2,1,3,4(communicated in earlier email).
You may exclude portions pertaining to catalyst and
statistical optimization (Response surface method) in
paper 3 and paper 4.

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