Tubular Reactors

Abstract

The article contains sections titled: 1. Introduction 2. Olefin Production by Steam Cracking 2.1. Background 2.2. Chemistry of Olefin Production 2.3. The Reactor 2.4. Reactor Design 2.5. Heat Recovery 2.6. Control of the Reactor 2.7. Coking 2.8. Alternatives to the Tubular Reactor 3. Gas‐Phase Chlorocarbon Cracking Reactions 3.1. Reaction Description 3.2. Reaction Thermodynamics 3.3. Reaction Mechanism 3.4. Reactor Design and Operating Conditions 3.5. Reactor Modeling 3.6. Reactor Coking and Carbon Formation 4. Gas‐Phase Halogenation Processes 4.1. Reaction Description 4.2. Substitutive Chlorination Reactors 4.2.1. Reactor Modeling 4.2.2. Reactor Coking and Soot Formation 4.3. Substitutive Bromination Reactors 4.3.1. Reactor Design 4.3.2. Reactor Modeling 4.3.3. Reactor Coking and Carbon Formation 4.4. Perhalogenation Reactors 4.4.1. Reaction Description 4.4.2. Reactor Design and Operation 4.4.3. Reactor Modeling 4.4.4. Reactor Coking and Carbon Formation 5. Fundamental Modeling Approaches — An Evaluation 5.1. Thermal Decomposition of Ethane 5.2. Improving the Model 6. Conclusions

CR3 Communication: Red Mud – A Resource or a Waste?

“…The Ti-rich solid remaining can be further processed via chlorination. 11 Synchronous recovery of Al, Fe and Ti is investigated by a number of researchers. One method utilizes chlorination combined with fractional distillation to extract Fe and Ti from red mud.…”