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