Extraction of Biodiesel Using Jatropha

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    EXTRACTION OF BIODIESELEXTRACTION OF BIODIESEL

    USING JATROPHAUSING JATROPHA

    SUBMITTED BY: NAVEEN CHANDRU.V

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    INTRODUCTION:INTRODUCTION:Every year the demand of energy is increasing. If the demand

    continues at this rate in future we end up with the depletion ofconventional energy resources.

    We are very much dependent on the petroleum fuels like petrol,Diesel, etc,. So there should be an effort has been to develop thealternative sources to the petroleum diesel.

    Our seminar involves with regard to the manufacturing of Bio

    Diesel from various vegetable oil including Jatropha. A research hasbeen carried out on the manufacturing of Bio Diesel and comparisonmade w.r.t the petroleum diesel in respect of cost benefits &advantages.

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    What

    is Bio Diesel ?What

    is Bio Diesel ?

    Bio Diesel is methyl or ethyl ester of fatty acids made from virgin orused vegetable oils ( both edible & non-edible) and animal fats. Themain commodity sources for Bio Diesel in India can be non- edible

    oils obtained from plant species such as jatropha curcas (Ratanjyot),Pongamia Pinnata(Karanj), Calophyllum inophyllum(nagachampa),Hevca brasiliensis(Rubber) etc.

    Bio Diesel contains no petroleum, but it can be blended at any levelwith petroleum diesel to create a BioDiesel blend or can be used in its

    pure form. Just like petroleum diesel, BioDiesel operates incompression ignition (Diesel) engine, which essentially require verylittle or no engine modifications because BioDiesel has propertiessimilar to petroleum diesel fuels.

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    It can be stored just like the petroleum diesel fuel and hence does not

    require separate infrastructure. The use of BioDiesel in conventional

    diesel engines results in substantial reduction of unburned hydrocarbons,carbon monoxide & particulate matters. BioDiesel is considered clean

    fuel since it has no sulphur, no aromatics & has about 10% built-in

    oxygen, which helps it to burn fully. Its higher cetane number improves

    the ignition quality even when blended in the petroleum diesel B20 ( a

    blend of 20% by volume BioDiesel with 80% by volume petroleumdiesel) has demonstrated significant environmental benefits. Studies

    conducted with BioDiesel on engines have shown substantial reduction

    in particulate matter (25-50%). However, a marginal increase in nox (1-

    6%) is also reported. HC and CO emissions were also reported to be

    lower.

    USA uses B20 and B100 BioDiesel. France uses B5 as mandatory

    in all diesel fuel. It can be also be used as an additive to reduce the

    overall sulfur content of blend and to compensate for lubricity loss due to

    sulfur removal from diesel fuel.

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    How BioDiesel sav

    es energy ?How BioDiesel sav

    es energy ?India ranks sixth in the world in terms of energy demand accounting

    for 3.5% of world commercial energy demand in 2001. The energy

    demand is expected to grow at 4.8%. The demand of diesel (HSD) is

    increased from 39.81 million metric tons in 2001-02 to 52.32 million

    metric tons in 2006-07 @ 5.6% per annum. Our crude oil productionas per the tenth plan working fro up is estimated to hover around 33-

    34 million metric tons per annum even though there will be increases

    in gas production from 86 million standard cubic meters per day

    (2002-03) to 103 million standard cubic meters per day in (2006-07).

    The estimated BioDiesel requirements for blending with petroleumdiesel for the period 2001-2007 is given below :

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    Bio Diesel requirement for blendingBio Diesel requirement for blendingTable 1Table 1

    Year Diesel demand

    million tons

    Bio Diesel requirement for blending

    million tons

    @5% @10% @20%

    2001-02 39.81 1.99 3.98 7.9

    2002-03 42.15 2.16 4.32 8.6

    2003-04 44.51 2.28 4.56 9.1

    2004-05 46.97 2.35 4.70 9.4

    2005-06 49.56 2.48 4.96 9.9

    2006-07 52.33 2.62 5.24 10.48

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    AT YEAR 2001AT YEAR 2001--0303

    0

    12

    3

    4

    5

    67

    8

    9

    @5% @10% @20%

    2001-02 39.81

    2002-03 42.15

    Diesel in

    Million tons

    % of Blending of BioDiesel

    Chart 1

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    AT YEAR 2003AT YEAR 2003--0505

    0

    1

    2

    3

    4

    5

    6

    7

    8

    9

    10

    @5% @10% @20%

    2003-04 44.51

    2004-05 46.97Diesel in

    Million

    tons

    % of Blending of BioDiesel

    Chart 2

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    AT YEAR 2005AT YEAR 2005--0707

    0

    2

    4

    6

    8

    10

    12

    @5% @10% @20%

    2005-06 49.56

    2006-07 52.33

    Diesel in

    Million

    tons

    % of Blending of Bio Diesel

    Chart 3

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    Feasibility of producing BioDiesel as dieselFeasibility of producing BioDiesel as diesel

    substitute:substitute:

    Jatropha curcas has been found the most suitable tree specie for the

    reasons summarized below:

    It can be grown as a quick yielding plant even in adverse land situations Viz, degraded& barren lands under forest & non-forest use , dry & drought prone areas, marginal

    lands & as a agroforesty crop.

    The seeds of Jatropha are available during the non-rainy season.

    Raising Jatropha plant & its maintenance creates jobs for the rural poor, particularly the

    landless, in plantation and primary processing through expellers.

    It has multiple uses & after the extraction of oil from the seeds, the oil cake left behindcan be used for Bio Gas production & is excellent organic manure, the bio mass of

    Jatropha curcas enriches the soil & it can also be put to other uses.

    Retains soil moisture & improve land capability & environment.

    Jatropha adds to the capital stock of the farmers & the community, for sustainable

    generation of income & employment.

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    Country wise capacity ofthe BioDieselCountry wise capacity ofthe BioDiesel

    plantsplantsTable 3Table 3

    Country Number plants Total annual capacity

    000 tons

    Oils use

    Austria 11 56.2 to 60 Used frying oil

    Belgium 3 241

    Canada 1

    Czech republic 17 42.5 to 45 Used frying oil

    Denmark 3 32

    France 7 38.1

    Germany 8 207

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    Hungary 17 18.8

    Ireland 9 5 Used frying oil

    Italy 9 779 Sunflower oil

    Nicaragua 1 Jatropha

    Slovakia 10 50.5 to 51.5

    Spain 1 0.5

    Sweden 3 75

    Switzerland 1 2

    U.K 1

    U.S.A 40 190 Used frying oil

    Yugoslavia 2 5

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    PRINCIPLE AND DETAILED OPERATION OFPRINCIPLE AND DETAILED OPERATION OF

    BIODIESEL PRODUCTIONBIODIESEL PRODUCTION

    Reaction raw materials:

    1. Jatropha oil

    2. Methanol (CH3OH)99%+Pure

    3. Potassium hydroxide(must be dry)

    Materials for Titration:

    1. Isopropyl alcohol 99% + pure

    2. Distilled water

    3. Phenolphthalein solution (not more than a

    year old, kept protected from strong light)

    Chemical Reaction

    (CnHn+2)COOH + CH3OH= H3C-OOC(CnHn+2) +

    H2O

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    STEPS INVOVLED IN EXTRCTIONSTEPS INVOVLED IN EXTRCTION

    1. Filtering:

    Filter the oil to remove solid particles. You may have to warm it up

    a bit first to get it to run freely, 35 deg C should be enough.

    2. Removing the water :

    Heat the oil first to remove any water content. Waste oil will

    probably contain water, which can slow down the reaction & cause

    saponification( soap formation). The less water in the oil is better. Raise the

    temperature to 100 deg C, hold it there & allow any water to boil off. Run

    the agitator to avoid steam pockets forming below the oil & exploding,splashing hot oil.when boiling slows, raise the temperature to 130 deg C for

    10 min. Remove heat & allow cooling.

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    4. Basic titration:

    Dissolve 1 gram of KOH in 1 liter of distilled or de-ionized

    water (0.1% KOH solution). You can use phenolphthalein solution to get end

    point, in a smaller beaker, dissolve 1 ml of dewatered oil in 10 ml of pureisopropyl alcohol. Warm the beaker gently by standing it in some hot water, stir

    until all the oil dissolves in the alcohol and the mixture turns clear. Add 2 drops

    of phenolphthalein solution. Using a burette, add 0.1% KOH solution drop by

    drop to the oil alcohol phenolphthalein solution, stirring all the time, until the

    solution stays pink for 10 seconds. This is the number of grams of KOH you will

    need per liter of oil.

    5. Preparing the potassium methoxide:

    Generally the amount of methanol needed is 20% of the

    jatropha oil by mass. The densities of these liquids are fairly close, so 20% of

    methanol by volume should be about right. To be completely sure, measure out ahalf-liter of both fluids, weigh, & calculate exactly what 20% by mass is.

    Different oils can have different densities depending on what type of oil is

    originally was. The methanol is mixed in to a solution with the KOH, creating

    potassium methoxide in an exothermic reaction. Keep all utensils the KOH

    comes in contact with as dry as possible.

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    6. Heating & Mixing:

    Pre heat jatropha oil at 48-54 deg C & use a high speed propeller

    coupled to an electric motor to work as a mixer. Adjust the speed of stirrer to get the

    write effect of mixing & add the potassium methoxide to oil while stirring themixture. Stir the mixture for 50min-1 hr though the reaction will complete in 30 min.

    The reaction will be better if we take longer duration Methyl esters will be separated

    from the glycerin.

    7.

    Settling & Separation:Allow the solute to settle down for at least 8 hrs the Bio Diesel

    (Methyl esters) will be floating on top while the denser glycerin will settle down at

    the bottom of the container forming a hard gelatinous mass then care fully decant the

    Bio Diesel. Alternatively you can drained by using transparent holes from bottom of

    the container when glycerin gets solidified. If any Bio Diesel is left out the same can

    be taken out easily. When once the glycerin is solidified.

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    8. Glycerin :

    It is a Bi product during a process of manufacturing Bio Diesel which gets

    solidified below 38 deg C. Glycerin from fresh oil often remains liquid at a lower

    temperatures. Reclaim glycerin is composted by allowing methanol can be removedfor reuse by condensing the vapors through a condensers. Glycerin is a bi-product

    can be used for preparation of Medicines, Tinctures, Hand lotions, Wax e.t.c.

    9. Soap residue :

    The soapy residue suspended in a Bio Diesel due to the presence of Kpositive ions from the KOH can be removed by ensuring the dry contact surface for

    potassium hydroxide.

    10. Washing & Drying :

    After the soap residue is removed the Bio Diesel can be stored for about 2

    days to remove the left out soap residues to settle down before running the Bio

    Diesel through a filtration system in to the vehicle fuel tank. Another method is

    washing the Bio Diesel with any soap residue by using water for 2-3 times. Care

    must be taken to had a small amount of dilute acetic acid before adding the water

    which brings the PH value closer to the neutralization & drops out any suspended

    KOH.

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    COST ESTIMATION OF BIODIESELCOST ESTIMATION OF BIODIESELTABLETABLE

    Cost (Rs) Assumption/Remarks

    Cost of seed (Rs/Kg oil) 16.50 Seed Rs5/Kg. Oil yield 33% 3.28Kg seed for 1 Kg of oil

    Cost of collection & oil

    extraction

    2.48 Losses 5% I.e, 1.05 Kg for 1Kg of

    oil, extraction @ Rs.2.35/Kg

    Transesterification cost 7.00 For 1000 ltr/day

    Cost of BioDiesel 25.98

    Less Byproduct(oil Cake) -2.50 2.5 Kg cake at a cost of Rs.1/Kg

    Less Byproduct(Glycerol) -3.80 0,095 Kg at a cost of Rs40/Kg

    Net cost of BioDiesel per Kg 19.68 As per our estimation

    Net cost of BioDiesel per Ltr 16.73 Specific Gravity of oil is 0.85

    Sale price of BioDiesel 20.00 Profit 12%(Rs2/ltr) transport

    Rs.0.40/ltr & interest &

    miscellaneous Rs 0.87/ltr

    Cost of petroleum Diesel as

    in crude oil stage

    19.00 Excluding Excise/sales tax(based on

    $65/barrel crude)

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    COST OF PETROLEUM DIESELCOST OF PETROLEUM DIESELTABLETABLE

    Cost element Cost/liter Remarks

    Crude petroleum 24.00 CIF $ 65/BarrelCustoms duty 3.6 @15%

    Ocean loss 0.276 @1%

    Refinery transfer price 22.04Refinery & byproduct -0.45 Negative margins

    Basic selling price 27.88

    Road/Rail transport 0.45 Per liter

    Ex-Depot price 28.33

    VAT 3.25 @12%

    Dealer commission 0.67 @600/KL & cess 70/KL

    Selling price 30.78 @chennai

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    COMPARISION STUDY OF BIODIESEL FROMCOMPARISION STUDY OF BIODIESEL FROM

    VARIOUS SEEDS & PETROLEUM DIESEL INVARIOUS SEEDS & PETROLEUM DIESEL IN

    SINGLE CYLINDER ENGINE:SINGLE CYLINDER ENGINE:

    Sl.no Load on break drum(kg)

    Dead wt spring load

    Fuel

    consumption

    CC

    Time taken for to

    consume 10CC

    Fuel

    consumption

    (Kg/hr)

    Speed(rpm)

    1. 1.25 0 10 67 0.936 1575

    2. 4 1 10 51 1.244 1550

    3. 7.5 2 10 40 1.587 1525

    4. 9.85 4 10 34 1.867 1505

    5. 13,35 4.5 10 27 2.357 1475

    Economical speed test by using petroleum diesel:

    Economical speed test by using diesel:

    1. 1.25 0 10 72 0.962 1573

    2. 4 1 10 55 1.344 1545

    3. 7.5 2 10 42 1.617 1522

    4. 9.85 4 10 32 1.767 1501

    5. 13,35 4.5 10 30 2.157 1470

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    CONNCLUSIONCONNCLUSION

    BioDiesel has been manufactured successfully. The performance of the

    engine is better with the Bio Diesel compare with petroleum Diesel. It

    gives better better lubricating property and it emits very low quantity

    of carbon dioxide. It does not create any air pollution compare withpetroleum Diesel.

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