Page 19 - Analysis, Synthesis and Design of Chemical Processes, Third Edition

C.1.1 Background
C.1.2 Process Description of the Beaumont Allyl Chloride Facility
C.1.3 Specific Objectives of Assignment
C.1.4 Additional Background Information
C.1.5 Process Design Calculations
Fluidized Bed Reactor, R-601
C.1.6 Reference
Project 2 Design and Optimization of a New 20,000-Metric-Tons-per-Year Facility to Produce
Allyl Chloride at La Nueva Cantina, Mexico
C.2.1 Background

C.2.2 Assignment
C.2.3 Problem-Solving Methodology
Process Information
Project 3 Scale-Down of Phthalic Anhydride Production at TBWS Unit 700
C.3.1 Background
C.3.2 Phthalic Anhydride Production
C.3.3 Other Information
C.3.4 Assignment
C.3.5 Report Format
Project 4 The Design of a New 100,000-Metric-Tons-per-Year Phthalic Anhydride Production
Facility
C.4.1 Background

C.4.2 Other Information
C.4.3 Assignment
C.4.4 Report Format
Project 5 Problems at the Cumene Production Facility, Unit 800
C.5.1 Background
C.5.2 Cumene Production Reactions
C.5.3 Process Description
C.5.4 Recent Problems in Unit 800
C.5.5 Other Information
C.5.6 Assignment
C.5.7 Report Format
C.5.8 Process Calculations
Project 6 Design of a New 100,000-Metric-Tons-per-Year Cumene Production Facility
C.6.1 Background
C.6.2 Assignment
C.6.3 Report Format