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    Review I

    Group 35Remo Prathap

    Rashesh Gupta

    Yeswin Raja

    CO-PROCESSING OF

    JATROPHA OIL WITHLINEAR RUN DIESEL

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    Introduction

    The Process

    Comparison to Conventional Process Process Flow Diaram !aterial "alance #e$t %teps

    Contents

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    &atropha curcas is a species o' (owerin and 'ruit )earinplant in the enus &atropha*

    The seeds contain +,-./0 oil 1averae2 3.*.0 that can)e processed to produce a hih 4ualit "io-diesel 'uel6usa)le in a standard diesel enine*

    Co-processin technolo can )e deploed in an e$istinPetroleum Re7ner in'rastructure with minor modi7cationsand does not re4uire a separate plant*

    Indian 8il 9Indian 8il Corporation :imited; developed anew technolo to convert non-edi)le veeta)le oils tohdrocar)ons over indienous catalst6 which is a simple6sustaina)le6 economical and eco-'riendl process*

    Introduction

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    In this process6 trilcerides o' 'att acids contained in theveeta)le and

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    For either total material )alance or component material)alance we use a simple )asic 'ormula which ma )estated as2

    Input mass (ow rate 8utput mass (ow rate B Rate o'ccumulation

    $%teri%& '%&%nce

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    "asis2

    3/m3=* E

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    "asis2

    33m3=*1E.3+*>1E.331E.331E

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    @+ re4uired 'or the @+% Reaction 1=//0 conversion

    + B =/*+ L*.33 B */ L5 L

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    Total @+ re4uired 'or 50 conversion B ,3*3=. L=*+ L*.33 B 3.*5+ L

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    For 50 conversion2-

    @+% B =>=*+ /*5 B =,+*+/ L= /*5 B 5=* L/ L

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    t 8utlet2

    @+%2 =,+*+ L

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    There is no suchre4uirement*

    N$cess alcohol notproduced*

    #o lcerineproduced*

    #eutraliAation o' 'attacids not re4uired*

    Co-!rocessin"

    Re4uirement o' removal o' 'ree 'att acids 'or avoidin saponi7cationin su)se4uent steps*

    Recover o' e$cess alcohol used in the process 'or completeconversion*

    Removal and sale o' )-product raw lcerine*

    Hater washin is re4uired to remove the caustic emploed 'orneutraliAation o' 'ree 'att acids O this adds to the plant euent*

    Con(ention%&

    Co)!%rison to Con(ention%&

    Process

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    Nner "alance Process N4uipment Desin Instrumentation and Process Control Cost Nstimation Plant :aout

    !aterial @andlin and %a'et Conclusions

    Ne*t Ste!s