8
REACTORS By: Shaimaa Soarkati, CHBE446 Section: 0301 A. James Clark School of Engineering

REACTORS By: Shaimaa Soarkati, CHBE446 Section: 0301 A.James Clark School of Engineering By: Shaimaa Soarkati, CHBE446 Section: 0301 A.James Clark School

Embed Size (px)

Citation preview

REACTORSBy: Shaimaa Soarkati,

CHBE446

Section: 0301

A. James Clark School of Engineering

Constant Stirred Tank Reactor (CSTR)

Steady-state continuous flow of reactants (A) and Products (B). Well-mixed reactor, so exit stream has the same composition as reactants in the tank

Phases present:

Liquid, Gas-liquid, Solid-liquid

Advantages:

Continuous process

Maintainable temperature

Simple design

Easy to clean

Low operating cost

Disadvantages:

Low conversion per unit volume

CSTR Equations

Mole Balance:

-

At steady state,

Rate Law:

Conversion:

;

Note: The volume is also calculated by measuring the area under the CSTR curve

Plug Flow Reactor (PFR)

A long reactor tube with consisting of many “plugs”

Concentration changes down the reactor (length-wise)

No radial variation in reaction rate/ concentration

For large scale

Heterogeneous and homogeneous reactions (fast)

Advantages:

High conversion per unit volume

Efficient heat transfer

Continuous process

Easy maintenance

Typically contain catalyst

Disadvantages:

Poor temperature control

Undesired thermal gradients possible

Poor mixing (static mixers)

PFR Equations

Mole Balance:

-

At steady state,

V=

Rate law:

Conversion:

Stoichiometry:

BATCH REACTOR

Reactants are supplied via the top two holes on the reactor and nothing can be added or extracted while the reaction process occurs.

Can be heated or cooled via jacket

Small scale

Used mostly for pharmaceutical or fermentation processes

Advantages:

High conversion per unit volume

Can be used for multiple operations

Easy to clean

Disadvantages:

Varied product quality

High operation cost

Batch Reactor Equations

Mole Balance: -

No inflow or outflow,

Rate Law:

Conversion:

Stoichiometry: =

Heterogeneous Catalysis

Form of catalysis where the catalyst phase is different from the reactants

Adsorption is an essential first step in heterogeneous catalysis Molecule in gas phase binds to a liquid or

solid surface

Surface Reactions Langmuir-Hinshelwood mechanism

Rideal-Eley mechanism

Precursor mechanism

www.techrem.ruhr-uni-Bochum.de

http://cdn.comsol.com/wordpress/2015/02/Eley-Rideal-mechanism.png