material balance for multi-unit operations

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    Material Balance for

    Multi-Unit Operations

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    Process Flow sheet Flow Chart)

    1. Process Information: key properties data, market conditions, techniinformation, etc., are collected.

    2. Input /Output Diagram: All major inputs and outputs streams and thstoichiometric balances are illustrated, according to the potential chemipathways.

    3. Functions Diagram: All the major functions of the process and materiflow to and from those functions are specified. The functions include reacti

    boxes, separation boxes, finishing boxes, etc.

    4. Operations Diagram: Detail technologies used such as types of reactoperating conditions, etc. are specified.

    5. Process Flow sheet: Details for each function are described, ready to use.

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    Process Flowsheet Development

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    Function Diagram

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    Operation Diagram

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    Process Flow sheet

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    MB for Multiple Units Process

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    Example on MB for Multi-units Process

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    Recycle System

    The stream containing the recycled material is kno

    as a recycle stream.

    Because of relatively high cost of industrial feerecycle of unused reactants/feed is a commpractice.

    Recovery of catalyst, circulation of working fluidilution of process streams, control of procvariables, etc., are all reasons for applicationsrecycle system.

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    Recycle with Chemical Reaction

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    Bypass and Purging

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    Bypassing wastewater to waste Lagoon

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    Limiting reactant

    In practice a reactant may be used in excess of thestoichiometric quantity for various reasons. In this casthe other reactant is limiting i.e. it will limit the yield oproduct(s)

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    Excess reactant

    A reactant is in excess if it is present in a quantity

    greater than its stoichiometric proportion.% excess = [(moles supplied stoichiometric

    moles)/stoichiometric moles] x 100

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    Conversion

    Fractional conversion = amount reactant

    consumed/amount reactant supplied % conversion = fractional conversion x 100

    Note: conversion may apply to single pass reactorconversion or overall process conversion

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    Yield

    Yield = (moles product/moles limiting reactant

    supplied) x s.f. x 100

    Where s.f. is the stoichiometric factor = stoichiometrimoles reactant required per mole product

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    Multiple Reactions

    There are four basic type of multiple reactions: series, parallel, complex, and indepe

    Parallel reactions competing reaction)

    A

    k1

    k2 C

    B

    Series reactions consecutive reaction)

    Ak1 k2

    CB

    The reactant is consumed by two different reaction pathways to form different pro

    The reactant forms an intermediate product, where reacts further to form another

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    Complex reactions

    ECA

    DCBA

    OHHCCHOCHHC

    HCHOCHOHHC

    OHHCOHHC

    264342

    2352

    24252

    Involving a combination of both series and parallel reactions

    Independent reactions

    FED

    CBA

    42143188

    6324123215

    HCHCHC

    HCHCHC

    Occurring at the same time but neither the products nor reactants react with thems

    or one another.

    formation of butadiene from ethanol

    cracking of crude oil to form gasoline

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    Selectivity tells us how one product is favored over another when we ha

    multiple reactions. We can quantify the formation of Desired product (D

    with respect to Undesired product (U) by defining the selectivity and yie

    of the system.

    The instantaneous selectivity of D with respective to U is the ratio of the rate

    formation of D to the rate of formation of U.

    UDS

    /

    ~

    Overall selectivity

    Selectivity

    / =

    =

    =

    =

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    Selectivity

    Selectivity = (moles product/moles reactant converted) x s.f. x

    OR

    Selectivity = moles desired product/moles byproduct

    Where s.f. is the stoichiometric factor = stoichiometric moles reactant re

    mole product

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    Selectivity and YieldInstantaneous Overall

    Selectivity:

    Yield:

    Example: desired product ,

    undesired product ,

    To keep the selectivity of the desired products high withrespect to the undesired products, carry out the reactioat high concentration of A and low concentration of B. Ahigh selectivity can easily be achieved in a semibatchreactor where B is fed slowly compared to A.

    rD k

    1CA

    2CB

    rU k

    2CACB

    2