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CONTENTSFront MatterCourse UnitsI. Chemical Reactions
II. Chemical Reaction Kinetics
A. Rate Expressions
B. Kinetics Experiments
C. Analysis of Kinetics Data
III. Chemical Reaction Engineering
A. Ideal Reactors
B. Perfectly Mixed Batch Reactors
C. Continuous Flow Stirred Tank Reactors
D. Plug Flow Reactors
E. Matching Reactors to Reactions
IV. Non-Ideal Reactions and Reactors
A. Alternatives to the Ideal Reactor Models
B. Coupled Chemical and Physical Kinetics
Supplemental Units |
Unit 18. Reaction Engineering of Batch ReactorsThis website provides learning and teaching tools for a first course on kinetics and reaction engineering. Here, in Part III of the course, the focus is on the modeling of chemical reactors. In particular, it describes reaction engineering using the three ideal reactor types: perfectly mixed batch reactors, continuous flow stirred tank reactors and plug flow reactors. After considering each of the ideal reactor types in isolation, the focus shifts to ideal reactors that are combined with other reactors or equipment to better match the characteristics of the reactor to the reactions running within it. Section B of Part III examines reaction engineering for perfectly mixed batch reactors. Typical reaction engineering tasks involving batch reactors are identified and described. In order to become a proficient reaction engineer, one must develop an intuitive appreciation of how a reactor responds to changes in operational procedures. For this reason a detailed discussion of the qualitative analysis of batch reactors is presented in this section along with the full mathematical analysis of their behavior. Unit 18 describes some of the more common reaction engineering tasks that involve batch reactors. It also describes how to qualitatively analyze a batch reactor. This is an important skill for a good reaction engineer to master. An intuitive, physical understanding of why the temperature, pressure, composition, etc. change in the way they do for a given combination of reaction, reactor and reactor operating procedure can prove invaluable when troubleshooting a problematic reactor or when setting out to design a new one. Unit 18 shows that it is possible to predict, at least qualitatively, many things about reactor performance without ever solving the design equations. Learning Resources
Teaching Resources
Practice Problems1. Consider a typical reaction that is reversible and exothermic. Suppose that reaction is run two separate times using a batch reactor. The reactor volume, initial composition and initial temperature are the same in both of the runs. One run is conducted isothermally and the other is conducted adiabatically. Sketch the conversion versus time for the two runs on the same set of axes. Your sketch should be sufficiently detailed to show initial and final slopes, curvature, inflection points, etc. If your artistic skills are weak, you should provide a brief written description of the two curves that describes these aspects. 2. Consider the exothermic, reversible reaction A → B. The reaction is first order in both directions. Suppose the reaction was run isothermally at each of two different temperatures. The initial concentration of A was the same in both runs and there was no B present initially in either run. (a) Sketch the concentration of A as a function of time for both runs on the same set of axes. (b) Sketch the fractional conversion of A as a function of time for both runs on the same set of axes. |