Chemical Reaction EngineeringReaction Mechanism and Kinetics Catalyst and Reactor Design Material, Energy and Momentum Balances Chemical engineering processes, Thermodynamics and fluid
Trang 1Chemical Reaction Engineering
Reaction Mechanism and Kinetics
Catalyst and Reactor Design
Material, Energy and Momentum Balances
Chemical engineering processes, Thermodynamics and fluid mechanics
Transport Kinetics
Mass and heat transfer
Scale-up
Scale-up of technical reactor
Reactor Operation and Control
Control of reactor processes
atomic level pellet level laboratory level production level atomic level pellet level laboratory level production level
Trang 4(RO)2 Si Si(OR)2
Trang 5Si OSi SiO SiO
Si OSi SiO
Si OSi SiO
Si OSi SiO
Si OSi SiO
Si OSi SiO SiO
Si OSi SiO SiO
Si OSi SiO
Si OSi SiO
agglomerates powder
Chemical Transformation -2
Sol-gel Process
Silica nanoparticles
Crystallization?
Trang 6Solar Energy Conversion in Chloroplast
Trang 7Catalyst speed up the rate of reaction by lowering the activation
energy (Ea)
It does not change the thermodynamics of the reaction,
It equally speed up the forward and reverse reactions,
It may undergo transformation during reaction, but is not
consumed by the reaction
(1.5) What are the other characteristics of a catalyst?
Trang 9Reactions occurs on the catalyst surface, therefore
a large surface area is advantageous
Trang 10Surface: XPS, AES, SIMS, FTIR
Localized: EDXS, EPM
Electronic
ESR, UV-Vis, IR, XPS
Screening Combinatorial screening Laboratory Reactor Batch, differential and integral In-situ Reaction
Reaction conducted under direct observation
CENG 511 (Spring 04)
Trang 11Sintering Clay Intercalation Microfabrication Thin film processes Polymerization Chemical Grafting Ligand Chemistry Enzyme and Proteins Etc…
Biological Catalysts
Enzymes
Catalase
(1.7) Give five more enzymes and the
reactions that they catalyzes
Trang 12System
Trang 13Material Balances
A government population survey of a new town shows that in a year 15,000 people establish residence in the town but during the same year 5000 people moves to the surrounding suburbs 8000 birth and 2000 death was recorded during the year How many people live in the city if the last year population is 350,000 people How many women in the city if the average male-female ratio is 0.82
Trang 14Accounts for chemical reaction
Trang 15Material Balances
Batch Reactor
Trang 16Experiment conducted using methanol solvent,
Large excess of 1-pentene was used,
Reaction conducted at room temperature.
= k’cA
Trang 17(1.8) Derive the reaction equation for a second order reversible reaction (A
to 2B) Plot CA/CA0vs reaction time
Trang 18Material Balances
Determine the concentration of 1-epoxypentene product
Trang 23Batch Reactor
Trang 24Energy Balances
General Energy Balance Equation for Batch Reactor
Heat of Reaction Sensible Heat
Expansion term Latent Heat
Trang 25Energy Balances
General Energy Balance Equation for Batch Reactor
Heat of Reaction Sensible Heat
Expansion term Latent Heat
Energy Balances
Heat of Reactions
Heat associated breaking and forming of chemical bonds in a molecule
Trang 27Energy Balances
Standard Heat of Combustion
Energy Balances
Constant Pressure
Trang 28Energy Balances
Constant Volume (Ideal Gas)
(2.1) Derive the above equation from the general energy balance equation for a batch reactor
Energy Balances
Constant Volume vs Constant Pressure
Trang 29Energy Balances
Liquid phase batch reactor – 1
The exothermic elementary liquid phase reaction:
was carried out in a batch reactor with a cooling coil to keep the reactor isothermal at 27C The reactor was filled with 2 mol/L of reactant A
(a) How long does it take to reach 95 % conversion?
(b) What is the total amount of heat (kcal) removed by the cooling coil when this conversion is reached?
(c) What is the maximum rate by which the heat must be removed by the heating coil (kcal/min) and at what time does this maximum occurs?(d) What is the adiabatic temperature rise for this reactor and its
significance?
Trang 30Energy Balances
Additional information:
Liquid phase batch reactor – 2
(2.2) Repeat the calculation for a second order irreversible reaction:
Trang 32Energy Balances
Adiabatic Heating and Temperature Rise
.
0 100 200 300
Trang 33Why study chemical reaction equilibrium when operating reactors
are never at chemical equilibrium?
Chemical Reaction Equilibrium
(1) Determine the limits of reactor performance,
(2) Explore possible design and operation changes that overcomes
these restriction and optimizes reactor performance
Thermodynamics
Gibbs Energy (∆G)
Physical and Chemical Precondition for Biochemical Reactions
including Cell Metabolism and Enzymatic Catalysis
Trang 34∆G < 0 Spontaneous, Energy releasing process –Exergonic Process
∆G = 0 Equilibrium process
∆G > 0 Non-spontaneous, Energy consuming process – Endergonic Process
Energy (Photon, Heat)
Nutrient (Reduced molecules)
cell metabolism
STORED ENERGY
Trang 37Condition for Reaction Equilibrium
The Gibbs free energy:
Extend of Reaction
Thermodynamics
Condition for Reaction Equilibrium
The Gibbs free energy:
Extend of Reaction
Trang 38Condition for Reaction Equilibrium
Necessary condition for reaction equilibrium
Standard Gibbs energy
activity fugacity
Thermodynamics
Condition for Reaction Equilibrium
The Gibbs free energy for a reaction system:
Standard Gibbs energy
of change
Equilibrium constant
Trang 39Ideal Gas Equilibrium – 1
High octane fuel additives are produced by reaction of isobutane with 1-butene hydrocarbons:
Determine the equilibrium composition of the reaction mixture at a pressure of 2.5 atm and temperature of 400 K The standard Gibbs
energy change for this reaction at 400 K is –3.72 kcal/mol
Assume that equimolar amounts of isobutane and 1-butene are present
in the initial mixture
(2.3) Please repeat the calculation if the initial ratio of I/B = 100, 10, 0.1