Batch Reactor 224

Embed Size (px)

Citation preview

  • 8/2/2019 Batch Reactor 224

    1/19

    WAQAR AHMAD NASEER

    2009-CH-224

  • 8/2/2019 Batch Reactor 224

    2/19

    Contents

    Selection of Batch reactors.

    Kinetics of Batch reactors.

    Calculations i.e. (different balances, residencetime e.t.c.)

    Designing the reactor on the basis of these

    calculations.

  • 8/2/2019 Batch Reactor 224

    3/19

    Why we need a Batch Reactor?

    Commonly said..

    Because we need high conversion per unit

    volume

    Is it the main character while choosing the

    B.rs????

    But the conversion per unit timedecreases!!!!

  • 8/2/2019 Batch Reactor 224

    4/19

    Main reason

    1.The reactants feed for B.rs is usually a

    catalyst+ reactants

    The catalytic reactions are usually of timeconsuming and need high residence time.

    So the choice of B.rs for these kind of

    reactions is perfect.2. Where small volumes of high-value products

    are made.

  • 8/2/2019 Batch Reactor 224

    5/19

    Kinetics of B.rs

    In a batch reactor the reactants and the catalystare placed in the reactor and the reaction isallowed to proceed for a given time whereupon

    the mixture of un reacted material togetherwith the products is withdrawn.

    In an ideal batch reactor, the concentrationand temperature are assumed to be uniform. Inpractice, the condition can be approximately

    realized by vigorous agitation or stirring.

  • 8/2/2019 Batch Reactor 224

    6/19

    Cont.

    All the elements of the fluid spend the sameamount of time in the reactor, and hence have

    the same residence time.Some of the reactions like enzyme reactions,are exothermic hence the temperaturecontrolling is an important phenomenon.

    Due to the presence of catalyst (enzyme e.t.c)the controlling of reaction conditions is muchmore difficult than other reactors.

  • 8/2/2019 Batch Reactor 224

    7/19

    Reaction kinetics and calculations:

    Considering an enzyme reaction occurring inside the

    reactor.

    the rate equation given by (Michaels & Menten)

    Dr/dt =k3*[A] [ Eo] / [M]+[A]

    Rate depends

    1.Enzyme

    2.Concentration of A if [A]M]

  • 8/2/2019 Batch Reactor 224

    8/19

    Designing the batch reactors

  • 8/2/2019 Batch Reactor 224

    9/19

    Before designing we must know.

    Agitation and cooling media selection

    Kinetics of reaction i.e. rate of reaction e.t.c.

    Enzyme characteristics i.e. (temperaturepressure controlling)

    Reaction feasibilities i.e. (temperature e.t.c

    requirements)Phases involving

    Residence time

  • 8/2/2019 Batch Reactor 224

    10/19

    Mixing and cooling media selection

    This depends upon the reaction conditionsand requirements:

    Agitation should be proper and at steadystate so not to interrupt the enzymemechanism

    Cooling depends upon the heat ofreaction, must be enough to remove theheat fro the vessel but not freezing it.

  • 8/2/2019 Batch Reactor 224

    11/19

    Kinetics of reaction

    Idea of rate of reaction

    Variations on reaction by changingtemperature pressure conditions.

    Heat of reaction to be remove from thereactor

    Effects of heat changing on reactionefficiency

  • 8/2/2019 Batch Reactor 224

    12/19

    Enzyme characteristics &Reaction

    feasibilities

    The reaction should be controlled in sucha way that enzyme should be free to do

    his work.The feasibility of reaction should also beaccounted to increase the efficiency

  • 8/2/2019 Batch Reactor 224

    13/19

    Phases involved

    They may be liquid, solid or gaseousphases present, some time the gaseousproduct is important and some time the

    liquid or solid.

    So there should be a proper mechanism toget our product safely and precisely from

    the reactor.

  • 8/2/2019 Batch Reactor 224

    14/19

    Residence time

    Important to find the range of conversionsof reaction.

    To find the completion time required tocomplete the reaction

  • 8/2/2019 Batch Reactor 224

    15/19

    Calculating the residence of reaction

    Considering a general reaction and applying

    the mole balance

  • 8/2/2019 Batch Reactor 224

    16/19

    Cont.

    Conversion X=Na/Nao

    dx=dNa/Nao

    dx/dt=dNa/dt.Naodx/dt=(dNa/dt.v).v/Nao

    dx/dt=-ra.v/Nao

    t=integral(0-x) dx.Nao/-ra.V

  • 8/2/2019 Batch Reactor 224

    17/19

    Complementary Equipments with

    batch reactors

    Heat Exchangers

    Sepration process

    Temprature and pressure control

    Pumps e.t.c

  • 8/2/2019 Batch Reactor 224

    18/19

  • 8/2/2019 Batch Reactor 224

    19/19

    QUESTIONS