BTC Biodiesel Workshop Session 2 (1)

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    BTC PTEC Biodiesel

    Workshop

    August 7 8, 2006

    Session 2 Chemical Background

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    Agenda for second session

    Biodiesel production

    Chemistry background

    Chemical compounds Chemical reactions in the production of

    biodiesel

    Material balance

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    Biodiesel Production

    Transesterification

    Esterification

    Pretreatment

    Biodiesel

    Washing

    Biodiesel

    Stripping

    ASTM Quality

    Biodiesel

    Gums / Waxes / Insolubles

    Glycerine

    Neutralization

    Glycerine

    Stripping

    Glycerine

    Distillation

    USP Grade

    Glycerine

    Acid Catalyst

    Base Catalyst

    Water

    Oil, Fat or Grease Feedstock

    Methanol

    Methanol

    and Water

    Distillation

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    Chemical background

    Biodiesel is made from a reaction of a

    vegetable oil or animal fat with an alcohol

    This reaction is called transesterification

    and produces an ester plus a glycerol

    We will first look at some chemical

    structure for compounds of interest in the

    making of biodiesel

    Then we will look at the reaction

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    Chemical compounds

    Vegetable oils and animal fats (triacylglycerols)

    O

    CH2OCR1 O CHOCR2 O CH2OCR3

    R groups are from fatty acids

    of the form

    O

    HOCR

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    Chemical compounds

    Oils and fats are composed of Fatty acids

    Saturated fats (no double bonds, C C only)

    Good cetane numbers and stability

    Poor cold weather properties

    Unsaturated fats (one or more double bonds,

    C = C)

    Can be oxidized Better cold weather properties

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    Chemical compounds

    Fatty acids

    CH3(CH2)14COOHpalmitic acid

    CH3(CH2)16COOHstearic acid

    CH3(CH2)7-CH=CH-(CH2)7COOH oleic acid CH3(CH2)7-CH=CH-CH2-CH=CH-

    (CH2)4COOHlinoleic acid

    CH3(CH

    2)7-CH=CH-CH

    2-CH=CH-CH

    2-

    CH=CH-CH2-COOHlinolenic acid

    CH3(CH2)7-CH=CH-(CH2)11- COOH erucicacid

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    Chemical compounds

    Things that we will use to make biodiesel are: Alcohols

    CH3OHmethanol

    CH3CH2OHethanol

    CH3CH2CH2OHn-propanol

    OH

    CH3CHCH3iso-propanol

    Bases NaOHsodium hydroxide

    KOHpotassium hydroxide

    NaOCH3sodium methoxide (sodium methylate, 25% active agent inmethanol)

    (We can determine the amount of catalyst needed by titrating asample of the vegetable oil with a base)

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    Chemical compounds

    The reaction will produce:

    Glycerols

    CH2OH

    CHOH

    CH2OH O

    Soaps (Naor K)OC - R

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    Chemical compounds

    And the biodiesel products we want are:

    Esters (examples)

    O

    CH3-C-O-CH3methyl acetate (methyl ester)

    O

    CH2-C-O-CH2CH3ethyl acetate (ethyl ester)

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    Other products

    Soaps O O

    Na

    O

    C

    R

    CH2

    O

    CR

    Mono and diglycerides CHOH OCHOH

    Free fatty acids HO - C - R

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    The transesterification reaction

    O

    CH2OCR1 O CH2 - OH

    CHOCR2 + 3 CH3OH = 3 CH3OOCRi+ CHOH O CH2 - OHCH2OCR3

    Triacylglycerol + alcohol = mixture of fatty acid esters

    (biodiesel) + glycerol

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    Phases

    Biodiesel (upper phase)

    Contains esters and some methanol (60:40 split with

    glycerine phase)

    Water not soluble in this phase Glycerine (lower phase)

    Also contains contaminants such as soaps

    90+% of soap formed

    And unreacted chemicals 95+% of catalyst added

    Alcohol split with biodiesel phase

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    Fatty acid reactions

    Side reactions also occur such as:

    Reaction with base to form a soap

    RCOOH + KOH = RCOOK + H2O

    A pretreatment reaction we might use is a FA

    with acid catalyst (H2SO4) and methanol to form

    an ester

    RCOOH + CH3OH = RCOOCH3+ H2O

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    Reactions of esters

    Other side reactions may be:

    Reaction with bases in water or water to form

    free fatty acids and acylates

    O O

    XOH + RO-C-R = XOR + HO-C-R

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    Reaction considerations

    Need excess of reactant (100% molar excess of alcohol)

    a catalyst (acid or base)

    moderate temperature (60 - 65 deg C, 140 150 deg

    F) mixing

    residence time (2 - 4 hours)

    Problems may occur from the presence of

    Free glycerol (inhibits reaction) moisture (hydrolysis of FA esters at > 0.5%)

    excess catalyst (soap formation)

    free fatty acids (soap formation)

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    Biodiesel from high FFA feedstocks

    To remove free fatty acids (FFA) to

    prevent soaps, we can use

    Acid catalyzed esterification to reduce FFA to

    < 0.5 1% and follow this with

    Alkali catalyzed transesterification

    Or we can just let them form soaps and

    hope for the best (no emulsion formationand not too much loss of product)

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    Example mass balance

    Reactants 100 pounds of vegetable oil (canola)

    23 pounds of methanol (100% excess)

    0.4 pounds of sodium hydroxide

    Products 100 pounds of ester (assuming 100% yield more

    commonly it would be 75% for one step and 98% fortwo steps)

    11 pounds of glycerine

    12 pounds of methanol (unreacted)

    0.4 pounds of sodium hydroxide

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    Volume balance

    Reactants

    13 gallons of vegetable oil (canola)

    3.5 gallons of methanol (100% excess)

    Products

    13 gallons of ester

    1 gallon of glycerine

    1.7 gallons of methanol (unreacted)

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    Transesterification Material Balance

    Oil Feedstock

    100 lb

    Catalyst

    0.5 to 1.5 lb

    Methanol

    10 lb + excess

    Acid

    Water

    1 to 100 lbGlycerine Esters

    FFA

    0 to 1 lb

    Reaction and Separation

    WashingAcidulationWaste Water

    0 to 100 lb

    Excess Methanol

    50 to >99%Methanol Removal Methanol Removal

    Crude Glycerine

    10 lb (pure basis)

    Biodiesel

    95 to 100 lb

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    Other steps in production

    Water wash (1 100 pounds)

    Methanol recovery

    Glycerine recovery or disposal Water treatment and disposal

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    Alternative reactant comparison

    Alcohol Costs (methanol often cheapest)

    Ethanol may be more difficult to recover than methanol, alsoneed more but it is renewable

    Propanol and higher alcohol derived biodiesels have lower

    freezing points Base catalyst

    Sodium hydroxide most common in US due to lower cost

    Potassium hydroxide more effective and is common in Europe,residue can be used as a fertilizer

    Methoxides used for large scale operations (>5 milliongallons/year) do not form water, most active catalyst

    Acid catalyst (sulfuric acid), cheap, does not makesoaps, very slow reaction

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    Other chemical issues

    Extended storage (>1 year) to result in Oxidation (rancidity)

    Polymerization

    Reactions catalyzed by metals and favored by contact

    with air, water or sunlight Inhibited by anti-oxidants

    Microbial attack

    Polyunsaturated fatty acids most susceptible tooxidation

    Safety Chemicals (Methanol, base, acid)

    Disposal of wastes