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Prasanna R Kovath
Assistant Professor
Department of Biotechnology
St. Mary's College Thrissur
• Four main production methods
• Direct use and blending
• Micro emulsions
• Thermal cracking
• Transesterification
• Transesterification
• Most common production method
• Uses vegetable oils and animal fats as feed stocks
• The reaction of a fat or oil with an alcohol to form esters
(biodiesel) and glycerol
• Direct Use – simplest method, 80% of petroleum heat content, ready
available feed stock, viscosity too high, reactivity of unsaturated
hydrocarbons
• Microemulsions – Utilizes alcohol solvents to reduce viscosity, causes
carbon and laquer deposits on engine parts
• Thermal cracking – Yields both biodiesel and gasoline, biodiesel
produced similar to petroleum, negates emissions benefits
• Transesterification – can be used as a continuous process, more
easily meets biodiesel fuel standards, expensive alcohol catalyst
There are three basic routes to biodiesel production from oils and
fats:
• Base catalyzed transesterification of the oil.
• Direct acid catalyzed transesterification of the oil.
• Conversion of the oil to its fatty acids and then to biodiesel.
CHARACTERISTICS OF OILS AND FATS USED IN
BIODIESEL PRODUCTION
• The US Department of Energy indicates that a perfect biodiesel should
only comprise mono-unsaturated fatty acids.
• Monounsaturated fatty acids (MUFAs) are the best components for
biodiesel when considering the low temperature fluidity and oxidative
stability.
• However, biodiesel derived from vegetable oils or microbial lipids
always consists of significant amounts of polyunsaturated and
saturated fatty acids (SFAs) alkyl esters, which hampers its practical
applications.
• Therefore, the fatty acid composition should be modified to increase
MUFA contents as well as enhancing oil and lipid production.
CHARACTERISTICS OF ALCOHOLS USED IN
BIODIESEL PRODUCTION
• Alcohols that can be used in biodiesel production are those with short
chains,including methanol, ethanol, butanol, and amylic alcohol.
• The most widely used alcohols are methanol (CH3OH) and ethanol
(C2H5OH) because of their low cost and properties.
• Methanol : Most widely used, in spite of its toxicity.
• It is a substance of petrochemical origin.
• Ethanol : Less used, requires more complex production technology
and the reaction speeds are lower. It can be produced from biomass.
BIODIESEL PRODUCTION PROCESS
• Biodiesel is produced from vegetable oils or animal fats and an
alcohol, through a transesterification reaction.
• This chemical reaction converts an ester (vegetable oil or animal fat)
into a mixture of esters of the fatty acids that makes up the oil (or fat).
• Biodiesel is obtained from the purification of the mixture of fatty acid
methyl esters (FAME).
• A catalyst is used to accelerate the reaction,According to the catalyst
used, transesterification can be basic, acidic or enzymatic.
• The Transesterification process is the reaction of a triglyceride
(fat/oil) with an alcohol to form esters and glycerol.
• A triglyceride has a glycerine molecule as its base with three long
chain fatty acids attached.
• The characteristics of the fat are determined by the nature of the fatty
acids attached to the glycerine.
• The nature of the fatty acids can in turn affect the characteristics of
the biodiesel.
• During the esterification process, the triglyceride is reacted with
alcohol in the presence of a catalyst, usually a strong alkaline like
sodium hydroxide.
• The alcohol reacts with the fatty acids to form the mono-alkyl ester, or
biodiesel and crude glycerol.
• In most production methanol or ethanol is the alcohol used (methanol
produces methyl esters, ethanol produces ethyl esters) and is base
catalysed by either potassium or sodium hydroxide.
• Potassium hydroxide has been found to be more suitable for the ethyl
ester biodiesel production, either base can be used for the methyl ester.
• A common product of the transesterification process is Rape Methyl
Ester (RME) produced from raw rapeseed oil reacted with methanol.
MIXING OF ALCOHOLAND CATALYST
• The catalyst is typically sodium hydroxide (caustic soda) or potassium hydroxide
(potash).
• It is dissolved in the alcohol using a standard agitator or mixer.
• Reaction. The alcohol/catalyst mix is then charged into a closed reaction vessel
and the oil or fat is added.
• The system from here on is totally closed to the atmosphere to prevent the loss of
alcohol.
• The reaction mix is kept just above the boiling point of the alcohol (around 160
°F) to speed up the reaction and the reaction takes place,varies from 1 to 8 hours,
and some systems recommend the reaction take place at room temperature. Excess
alcohol is normally used to ensure total conversion of the fat or oil to its esters.
• Care must be taken to monitor the amount of water and free fatty acids in the
incoming oil or fat.
• If the free fatty acid level or water level is too high it may cause problems with
soap formation and the separation of the glycerin by-product downstream.
SEPARATION
• Once the reaction is complete, two major products exist: glycerin and
biodiesel.
• Each has a substantial amount of the excess methanol that was used in
the reaction.
• The reacted mixture is sometimes neutralized at this step if needed.
• The glycerin phase is much more dense than biodiesel phase and the
two can be gravity separated with glycerin simply drawn off the
bottom of the settling vessel.
• In some cases, a centrifuge is used to separate the two materials faster.
ALCOHOL REMOVAL
• Once the glycerin and biodiesel phases have been separated, the excess
alcohol in each phase is removed with a flash evaporation process or
by distillation.
• In others systems, the alcohol is removed and the mixture neutralized
before the glycerin and esters have been separated.
• In either case, the alcohol is recovered using distillation equipment
and is re-used.
• Care must be taken to ensure no water accumulates in the recovered
alcohol stream.
GLYCERIN NEUTRALIZATION
• The glycerin by-product contains unused catalyst and soaps that are
neutralized with an acid and sent to storage as crude glycerin.
• In some cases the salt formed during this phase is recovered for use as
fertilizer.
• In most cases the salt is left in the glycerin. Water and alcohol are
removed to produce 80-88% pure glycerin that is ready to be sold as
crude glycerin.
• In more sophisticated operations, the glycerin is distilled to 99% or
higher purity and sold into the cosmetic and pharmaceutical markets.
METHYL ESTER WASH
• Once separated from the glycerin, the biodiesel is sometimes purified
by washing gently with warm water to remove residual catalyst or
soaps, dried, and sent to storage.
• In some processes this step is unnecessary. This is normally the end of
the production process resulting in a clear amber-yellow liquid with a
viscosity similar to petrodiesel.
• In some systems the biodiesel is distilled in an additional step to
remove small amounts of color bodies to produce a colorless biodiesel.
Biodiesel production

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Biodiesel production

  • 1. Prasanna R Kovath Assistant Professor Department of Biotechnology St. Mary's College Thrissur
  • 2. • Four main production methods • Direct use and blending • Micro emulsions • Thermal cracking • Transesterification • Transesterification • Most common production method • Uses vegetable oils and animal fats as feed stocks • The reaction of a fat or oil with an alcohol to form esters (biodiesel) and glycerol
  • 3. • Direct Use – simplest method, 80% of petroleum heat content, ready available feed stock, viscosity too high, reactivity of unsaturated hydrocarbons • Microemulsions – Utilizes alcohol solvents to reduce viscosity, causes carbon and laquer deposits on engine parts • Thermal cracking – Yields both biodiesel and gasoline, biodiesel produced similar to petroleum, negates emissions benefits • Transesterification – can be used as a continuous process, more easily meets biodiesel fuel standards, expensive alcohol catalyst
  • 4. There are three basic routes to biodiesel production from oils and fats: • Base catalyzed transesterification of the oil. • Direct acid catalyzed transesterification of the oil. • Conversion of the oil to its fatty acids and then to biodiesel.
  • 5. CHARACTERISTICS OF OILS AND FATS USED IN BIODIESEL PRODUCTION • The US Department of Energy indicates that a perfect biodiesel should only comprise mono-unsaturated fatty acids. • Monounsaturated fatty acids (MUFAs) are the best components for biodiesel when considering the low temperature fluidity and oxidative stability. • However, biodiesel derived from vegetable oils or microbial lipids always consists of significant amounts of polyunsaturated and saturated fatty acids (SFAs) alkyl esters, which hampers its practical applications. • Therefore, the fatty acid composition should be modified to increase MUFA contents as well as enhancing oil and lipid production.
  • 6. CHARACTERISTICS OF ALCOHOLS USED IN BIODIESEL PRODUCTION • Alcohols that can be used in biodiesel production are those with short chains,including methanol, ethanol, butanol, and amylic alcohol. • The most widely used alcohols are methanol (CH3OH) and ethanol (C2H5OH) because of their low cost and properties. • Methanol : Most widely used, in spite of its toxicity. • It is a substance of petrochemical origin. • Ethanol : Less used, requires more complex production technology and the reaction speeds are lower. It can be produced from biomass.
  • 7. BIODIESEL PRODUCTION PROCESS • Biodiesel is produced from vegetable oils or animal fats and an alcohol, through a transesterification reaction. • This chemical reaction converts an ester (vegetable oil or animal fat) into a mixture of esters of the fatty acids that makes up the oil (or fat). • Biodiesel is obtained from the purification of the mixture of fatty acid methyl esters (FAME). • A catalyst is used to accelerate the reaction,According to the catalyst used, transesterification can be basic, acidic or enzymatic.
  • 8.
  • 9. • The Transesterification process is the reaction of a triglyceride (fat/oil) with an alcohol to form esters and glycerol. • A triglyceride has a glycerine molecule as its base with three long chain fatty acids attached. • The characteristics of the fat are determined by the nature of the fatty acids attached to the glycerine. • The nature of the fatty acids can in turn affect the characteristics of the biodiesel.
  • 10. • During the esterification process, the triglyceride is reacted with alcohol in the presence of a catalyst, usually a strong alkaline like sodium hydroxide. • The alcohol reacts with the fatty acids to form the mono-alkyl ester, or biodiesel and crude glycerol. • In most production methanol or ethanol is the alcohol used (methanol produces methyl esters, ethanol produces ethyl esters) and is base catalysed by either potassium or sodium hydroxide. • Potassium hydroxide has been found to be more suitable for the ethyl ester biodiesel production, either base can be used for the methyl ester. • A common product of the transesterification process is Rape Methyl Ester (RME) produced from raw rapeseed oil reacted with methanol.
  • 11. MIXING OF ALCOHOLAND CATALYST • The catalyst is typically sodium hydroxide (caustic soda) or potassium hydroxide (potash). • It is dissolved in the alcohol using a standard agitator or mixer. • Reaction. The alcohol/catalyst mix is then charged into a closed reaction vessel and the oil or fat is added. • The system from here on is totally closed to the atmosphere to prevent the loss of alcohol. • The reaction mix is kept just above the boiling point of the alcohol (around 160 °F) to speed up the reaction and the reaction takes place,varies from 1 to 8 hours, and some systems recommend the reaction take place at room temperature. Excess alcohol is normally used to ensure total conversion of the fat or oil to its esters. • Care must be taken to monitor the amount of water and free fatty acids in the incoming oil or fat. • If the free fatty acid level or water level is too high it may cause problems with soap formation and the separation of the glycerin by-product downstream.
  • 12. SEPARATION • Once the reaction is complete, two major products exist: glycerin and biodiesel. • Each has a substantial amount of the excess methanol that was used in the reaction. • The reacted mixture is sometimes neutralized at this step if needed. • The glycerin phase is much more dense than biodiesel phase and the two can be gravity separated with glycerin simply drawn off the bottom of the settling vessel. • In some cases, a centrifuge is used to separate the two materials faster.
  • 13. ALCOHOL REMOVAL • Once the glycerin and biodiesel phases have been separated, the excess alcohol in each phase is removed with a flash evaporation process or by distillation. • In others systems, the alcohol is removed and the mixture neutralized before the glycerin and esters have been separated. • In either case, the alcohol is recovered using distillation equipment and is re-used. • Care must be taken to ensure no water accumulates in the recovered alcohol stream.
  • 14. GLYCERIN NEUTRALIZATION • The glycerin by-product contains unused catalyst and soaps that are neutralized with an acid and sent to storage as crude glycerin. • In some cases the salt formed during this phase is recovered for use as fertilizer. • In most cases the salt is left in the glycerin. Water and alcohol are removed to produce 80-88% pure glycerin that is ready to be sold as crude glycerin. • In more sophisticated operations, the glycerin is distilled to 99% or higher purity and sold into the cosmetic and pharmaceutical markets.
  • 15. METHYL ESTER WASH • Once separated from the glycerin, the biodiesel is sometimes purified by washing gently with warm water to remove residual catalyst or soaps, dried, and sent to storage. • In some processes this step is unnecessary. This is normally the end of the production process resulting in a clear amber-yellow liquid with a viscosity similar to petrodiesel. • In some systems the biodiesel is distilled in an additional step to remove small amounts of color bodies to produce a colorless biodiesel.