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"Fueling the Future:
The Power of
Biodiesel"
Training on Biodiesel preparation in CBBS lab
PRESENTERS :Hinal Kuntar
Akash singh
TRAINERS : Prof.S.S Kachhwaha
: Dr. Pravin Kodgire
: Mr. Suvik Oza
: Mr. Chinmay Mathur
TABLE OF CONTENT
• Introduction
• Different types of Feed Stock & oil
Characterization
• Property of feed stock
• Esterification and transesterification
• Post Treatment Processes
• Different types of heterogenous catalyst
preparation
• Biodiesel Characterization as per ASTM
INTRODUCTION
• Biodiesel is a renewable,
biodegradable fuel that is a cleaner-
burning alternative to petroleum-
based diesel fuel.
• It is produced from renewable sources
like vegetable oils, animal fats, and
waste cooking oil.
• BIODIESEL YIELD CALCULATION :
Net biodiesel weight x % FAME GC
given oil weight
• Feed Stock :
• 1st generation: Edible oil - soybean oil, sunflower, corn,
olive, and coconut oils.
• 2nd generation: Non-Edible oil - Acid oil, Fatty Acid, Wax,
Sterin, Spent Earth, Soap Stock, Castor Oil, Karanja oil,
Kusum Oil, Mahua oil, Residue Oil, Rice Bran Non Edible
Oil, Sludge Oil, Neem oil
• 3rd generation: Animals Fat, Fish Oil And Algae
• 4th generation: Micro-feedstocks
FEED STOCK & OIL CHARACTERIZATION
PROPERTIES OF Feedstock
• FORMULA:
• FFA(FREE FATTY ACID) = ACID VALUE X (0.5 to 0.75)
• We are considering only 0.5
• FFA ( FREE FATTY ACID ) : For castor Oil FFA is 3.5
• So Acid Value will be 1.75 mg KOH/gram of oil
Acid Value should be less than 2%.
• Transesterification is the catalyzed reaction of oil or fat
with alcohol to yield an ester and glycerol
ESTERIFICATION :
• Esterification is the process of combining an organic acid
(RCOOH) with an alcohol (ROH) to form an ester (RCOOR) and
water.
TYPES OF REACTION
TRANS - ESTERIFICATION :
Alcoholic Solvent
(Methanol , Ethanol , Propanol etc. can be used) but
we used methanol for the economic purpose
• SOLVENTS :
SOLVENT & CATALYST USED
• CATALYST :
• For Esterification we used H2SO4 as a Catalyst and the
catalyst loading is 1.5 %
• For Transesterification we used KOH as a Catalyst with the
catalyst loading of 1 %
• CONVENTIONAL METHOD : Taking a Batch of 50g castor oil and
mixture of 17.1 g Methanol and g H2SO4 is prepared. Molar Ratio 1:10
Then after
SYNTHESIS OF BIODIESEL(Esterification)
MECHANICAL STIRRER
FOR PROPER REACTION
ROTARY FLASH EVAPORATOR
FOR METHANOL RECOVERY
KEPT IN SEPERATIONG FUNNEL TO
SEPARATE BIODIESEL
fu
• CONVENTIONAL METHOD :
SYNTHESIS OF BIODIESEL
Washing with Di-Water Removing Moisture by Magnetic Stirrer
Then collect it in different
Glassware
We didn’t get Biodiesel from this
because there is less presence of
FFA in the oil and also this
technique is less effective
SYNTHESIS OF BIODIESEL (TRANSESTERIFICATION)
High Speed Grinder
ROTARY FLASH EVAPORATOR FOR
METHANOL RECOVERY
SEPARATING THE MIXTURE
From high Speed Grinder : Taking a Batch of 255g Karanja oil and mixture of 52g Methanol and
2.5 g KOH is prepared. Molar Ratio is 1:6.
HETEROGENEOUS CATALYST SYNTHESIS
Cao (Calcium Oxide) From Egg Shell
Fe3O4(Ferrous Oxide) From FeCl2 And FeCl3
Srx/Fe3-xO4 From Strontium Nitrate
By Co-Precipitation Method
Preparation of SRx 2gm Fe3O4 Mixed With 30 ml Di- Water, Putting it in Magnetic Stirred
for 20 Minutes, then Add Solution of Strontium Nitrate of 0.731 gm in 20 ml dropwise,
Maintain Temperature at 90 Celcius, then we added Ammonium Hydroxide for
Precipitation And Kept for 2 Hours.
Drying Process at 120 °C
Remi Centrifuge at 3000 RPM
• KARL FISCHER TITRATOR
ASTM D6304
BIODIESEL CHARACTERIZATION AS
PER ASTM/EN
• BOMB CALORIMETRY
ASTM D4868
• VISCOSITY METER
ASTM D445
• Pour Point -15.3 °C
• Cloud point -12 °C
BIODIESEL CHARACTERIZATION AS
PER ASTM/EN
Pour Point and Cloud Point
Tester
FOR LARGE SCALE PRODUCTION :
• SHOCK WAVE REACTOR
• HYDODYNAMIC
CAVITAION
REACTOR
• PI SEQUENTIAL REACTOR
CAPACITY : 100 LITRES PRODUCTION OF BIODIESEL
PLANT VISIT
THANK YOU

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5_Days_Hands_on_workshop_on_biodiesel_g4[1].pptx

  • 1. "Fueling the Future: The Power of Biodiesel" Training on Biodiesel preparation in CBBS lab PRESENTERS :Hinal Kuntar Akash singh TRAINERS : Prof.S.S Kachhwaha : Dr. Pravin Kodgire : Mr. Suvik Oza : Mr. Chinmay Mathur
  • 2. TABLE OF CONTENT • Introduction • Different types of Feed Stock & oil Characterization • Property of feed stock • Esterification and transesterification • Post Treatment Processes • Different types of heterogenous catalyst preparation • Biodiesel Characterization as per ASTM
  • 3. INTRODUCTION • Biodiesel is a renewable, biodegradable fuel that is a cleaner- burning alternative to petroleum- based diesel fuel. • It is produced from renewable sources like vegetable oils, animal fats, and waste cooking oil. • BIODIESEL YIELD CALCULATION : Net biodiesel weight x % FAME GC given oil weight
  • 4. • Feed Stock : • 1st generation: Edible oil - soybean oil, sunflower, corn, olive, and coconut oils. • 2nd generation: Non-Edible oil - Acid oil, Fatty Acid, Wax, Sterin, Spent Earth, Soap Stock, Castor Oil, Karanja oil, Kusum Oil, Mahua oil, Residue Oil, Rice Bran Non Edible Oil, Sludge Oil, Neem oil • 3rd generation: Animals Fat, Fish Oil And Algae • 4th generation: Micro-feedstocks FEED STOCK & OIL CHARACTERIZATION
  • 5. PROPERTIES OF Feedstock • FORMULA: • FFA(FREE FATTY ACID) = ACID VALUE X (0.5 to 0.75) • We are considering only 0.5 • FFA ( FREE FATTY ACID ) : For castor Oil FFA is 3.5 • So Acid Value will be 1.75 mg KOH/gram of oil Acid Value should be less than 2%.
  • 6. • Transesterification is the catalyzed reaction of oil or fat with alcohol to yield an ester and glycerol ESTERIFICATION : • Esterification is the process of combining an organic acid (RCOOH) with an alcohol (ROH) to form an ester (RCOOR) and water. TYPES OF REACTION TRANS - ESTERIFICATION :
  • 7. Alcoholic Solvent (Methanol , Ethanol , Propanol etc. can be used) but we used methanol for the economic purpose • SOLVENTS : SOLVENT & CATALYST USED • CATALYST : • For Esterification we used H2SO4 as a Catalyst and the catalyst loading is 1.5 % • For Transesterification we used KOH as a Catalyst with the catalyst loading of 1 %
  • 8. • CONVENTIONAL METHOD : Taking a Batch of 50g castor oil and mixture of 17.1 g Methanol and g H2SO4 is prepared. Molar Ratio 1:10 Then after SYNTHESIS OF BIODIESEL(Esterification) MECHANICAL STIRRER FOR PROPER REACTION ROTARY FLASH EVAPORATOR FOR METHANOL RECOVERY KEPT IN SEPERATIONG FUNNEL TO SEPARATE BIODIESEL
  • 9. fu • CONVENTIONAL METHOD : SYNTHESIS OF BIODIESEL Washing with Di-Water Removing Moisture by Magnetic Stirrer Then collect it in different Glassware We didn’t get Biodiesel from this because there is less presence of FFA in the oil and also this technique is less effective
  • 10. SYNTHESIS OF BIODIESEL (TRANSESTERIFICATION) High Speed Grinder ROTARY FLASH EVAPORATOR FOR METHANOL RECOVERY SEPARATING THE MIXTURE From high Speed Grinder : Taking a Batch of 255g Karanja oil and mixture of 52g Methanol and 2.5 g KOH is prepared. Molar Ratio is 1:6.
  • 11. HETEROGENEOUS CATALYST SYNTHESIS Cao (Calcium Oxide) From Egg Shell Fe3O4(Ferrous Oxide) From FeCl2 And FeCl3 Srx/Fe3-xO4 From Strontium Nitrate By Co-Precipitation Method Preparation of SRx 2gm Fe3O4 Mixed With 30 ml Di- Water, Putting it in Magnetic Stirred for 20 Minutes, then Add Solution of Strontium Nitrate of 0.731 gm in 20 ml dropwise, Maintain Temperature at 90 Celcius, then we added Ammonium Hydroxide for Precipitation And Kept for 2 Hours.
  • 12. Drying Process at 120 °C Remi Centrifuge at 3000 RPM
  • 13. • KARL FISCHER TITRATOR ASTM D6304 BIODIESEL CHARACTERIZATION AS PER ASTM/EN • BOMB CALORIMETRY ASTM D4868 • VISCOSITY METER ASTM D445
  • 14. • Pour Point -15.3 °C • Cloud point -12 °C BIODIESEL CHARACTERIZATION AS PER ASTM/EN Pour Point and Cloud Point Tester
  • 15. FOR LARGE SCALE PRODUCTION : • SHOCK WAVE REACTOR • HYDODYNAMIC CAVITAION REACTOR • PI SEQUENTIAL REACTOR
  • 16. CAPACITY : 100 LITRES PRODUCTION OF BIODIESEL PLANT VISIT