Group b Presentation 3 Son

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    SCREENING ALTERNATIVES, FLOWSHEETING,

    PLANT LAYOUT AND DETAILED COST ANALYSES

    OF BIODIESEL PRODUCTION IN TURKEY

    Group B051145003 Glseren Akku

    051145011 Berkan Bayar

    051145016 ahin alar

    051145049 Buket Ylmaz

    061145049 Gkhan E. Nar

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    What is the aim of the project ?

    X Oil Company want to make decision on the contruction of the biodiesel plant

    Large Scale Plant

    By-product of glycerol evaluation

    What was done in this project ?

    Market Analysis,Technology Type Selection,

    By-product of glycerol evaluation

    Main and Auxiliary equipments design,

    Piping and Plant Layout,

    Detailed Economic Analysis

    Preparing a preliminary design for biodiesel production process

    Objective of this study is determine manufacturing cost and the capital investement

    What was the work in this project?

    What was wanted in this project?

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    Market Analysis in Turkey

    According to the Table, %5 of biodieselrequirement in diesel is 406.525 tons in 2007.

    Capacity of biodiesel plant is 27.000 tons/yearin Turkey by research.

    Capacity is determined as 40.000 tons/year. It

    is 10% of biodiesel market (%5 biodiesel indiesel).

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    BIODIESEL PRODUCTION TECHNOLOGIES

    Homogeneous Alkali (Base) Acid Catalyzed

    Transesterification

    Heterogeneous Acid and Base-Catalyzed

    Transesterification

    Enzymatic Transesterification

    Supercritical Alcohol Transesterification

    Microwave Assisted Transesterification

    Ultrasound Assisted Transesterification

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    0 10

    Homogeneous Catalysis Technology

    Heterogeneous Catalysis Technology

    Enzymatic Catalysis Technology

    Supercritical Technology

    Selecting Technology Type

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    Recommended Block Diagram of SCT

    Some Improvments Are Need

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    Improved Block Diagram of SCT

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    Process Flow Diagram of SCT

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    Design Basis

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    Material Balance

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    Energy Balance

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    Result of Material And Energy

    Balances

    0,04 $ is spending on energy and utilities per a kg of biodiesel

    0,43$ is spending on raw materials per 1 kg of product. This isnearly %70 of estimated selling price.

    Profitable to go on

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    Main Equipments Design

    Total =418474 $

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    Auxiliary Equipments Design

    Total = 735484 $

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    Introduction to Plant Layout

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    Piping Design

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    Piping Design Results

    Electrical Cost(EC) = 0,2784 $/kWh * 340 kW = 94,656 $/h

    Total length of pipe segment =580,5 m

    Cost of pipe: 580,5* 37,09 = 21530 $

    Purchased equipment cost (PEC) =500776,7 $

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    Detailed Economic Analysis

    Total= 418474 $ Total= 192436 $Total= 668638 $ Total= 53030,35 $/Y

    Main Equipments Analysis

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    Detailed Economic Analysis

    Auxiliary Equipments Analysis

    Total= 89943$Total= 1126284 Total= 220669$Total= 735484 $Total= 301633 $

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    Detailed Economic Analysis

    Utility Cost Analysis

    Total=74840000 $

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    TPC = 0.567198 $/kg

    TCI = 19222476 $FCI = 17300228 $

    Detailed Economic Analysis

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    Detailed Economic AnalysisProfibility Analysis

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    Result of Economic Analysis

    Profit is the goal of any investment. When the capacity reachs low ratio, raw material

    costs, utility costs will be low, also. But, taxes which is fixed cost can not change. By

    the time capacity is low, total income will be low. When total incomes and costs are

    calculated for each capacity, breakeven point can be determined which income and cost

    is equal to each other.According to depreciation, fixed capital investment and annual net profit, payout

    period was calculated as nearly six year. It is good result because the lenght of time is

    not long. It s necessary for the total return to equal the capital investment. We

    obtained that it is profitable process for 40000 tones/ year capacity at %75 capacity

    ratio according to results.