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Lecture 22 Thursday 3/27/08 Blowout Velocity CSTR Explosion Batch Reactor Explosion. CSTR with Heat Effects. Energy Balance for CSTRs Equation (8-9) (page 476). (page 593). At Steady State. Solving for X Solving for T. Mole Balance. Rate Law Stoichiometry Combine. Heat Effects.
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Lecture 22 Thursday 3/27/08Blowout VelocityCSTR ExplosionBatch Reactor Explosion
CSTR with Heat Effects Energy Balance for CSTRs Equation (8-9) (page 476)
At Steady State Solving for X Solving for T
Mole Balance Rate Law Stoichiometry Combine
Heat Effects Isothermal Design Stoichiometry Rate Laws Mole Balance
Isothermal Design Heat Effects Rate Laws Stoichiometry Mole Balance
Complete conversion FA = 0 • Batch Reactors with Heat Effects • Single Reactions • Multiple Reactions • Risk Rupture
Keeping MBAs Away From Chemical Reactors The process worked for 19 years before they showed up!! Why did they come???? What did they want????
NO2 NO2 Cl NH2 + 2NH3 + NH4Cl ONCB + Ammonia Nitroanaline + Ammonium Chloride Nitroaniline Synthesis Reaction
NH3 in H2O ONCB Autoclave 175 oC ~550 psi NH3 Separation Filter Press O-Nitroaniline Product Stream “fast” Orange Nitroaniline Synthesis Process To Crystallizing Tanks
Old 3 kmol ONCB 43 kmol Ammonia 100 kmol Water V = 3.25 m3 Nitroaniline Synthesis Reactor
NO2 NO2 Cl NH2 + 2NH3 + NH4Cl ONCB + Ammonia Nitroanaline + Ammonium Chloride Same Nitroaniline Synthesis Reaction Batch Reactor, 24 hour reaction time Management said:TRIPLE PRODUCTION
New 9 kmol ONCB 33 kmol Ammonia 100 kmol Water V = 5 m3 MBAStyle Nitroaniline Synthesis Reactor
400 Temperature oC Cooling Restored Isothermal Operation 200 175 9:55 t = 0 10:40 10:50 midnight 12:18 Temperature-time trajectory fuse
400 Temperature oC Cooling Restored Qr = 0 Isothermal Operation 200 175 9:55 t = 0 10:40 10:50 midnight 12:18 Temperature-time trajectory fuse
Example Mole balance) Rates) net rates, relative rates, rate laws….. Stoichiometry) Energy Balance)
FA0 FI0 A If the flow rate shut off, the temperature will rise (possibly to point of explosion!)