ETS/Theodore Tutorials
Process Synthesis and Design A Self-Instructional Problem Workbook
David Kauffman Chemical and Nuclear Engineering Department The University of New Mexico, Albuquerque NM
Published by ETS Professional Training Institute © 1992 Louis Theodore. 254 pages. ISBN 1-882767-08-X.
Table of Contents
Basic Operations Process Synthesis Known Processes · New Processes
Process Economics Capital Costs · Operating Costs · Overall Economics
Flow Sheets Block Diagrams · Process Flow Sheets · Piping and Instrumentation Diagrams
Continuous and Batch Operations Continuous Operations · Batch Operations
Material and Energy Balances Once-through Systems · Recycle Systems
Short-cut Equipment Design Methods Liquid Handling · Gas Handling · Solids Handling · Heating and Cooling · Chemical Reactions · Separations
Materials of Construction Strength of Materials · Corrosion · Comparative Costs
Utility Systems Steam Systems · Cooling Water · Other Utilities
Shipping and Storage Shipping Facilities · Tank Farms
Plant Layout Process Flow Approach · Common Equipment Approach
Process Control and Instrumentation Instrumentation and Measurement · Control Loops · Alarms and Trips · Computer Control
Plant Reliability Safety Factors in Design · Redundancy in Design
Plant Safety Fire and Explosion Hazards · Toxic Materials Hazards · Plant Safety Analyses · Operating Procedures
Worker Health and Safety Protective Equipment · Training · Operating Procedures
Environmental Controls Air Emissions · Toxic Air Emissions · Water Pollution Control · Solid Waste · Hazardous Waste
Problems Process Synthesis and Selection (PSS) PSS 1: Scale-up of a Lab Process: Sulfur Removal from Oil PSS 2: Scale-up of an Existing Process: Ethanol Synthesis PSS 3: Batch vs. Continuous Processing: Lube Oil Refining PSS 4: Material Balance, Once Through: BTX Separations PSS 5: Material Balance with Recycle: Toluene Disproportionation PSS 6: Energy Balance: Manufacture of Ammonia PSS 7: Material Balance: Accounting for By-Products
Process Economics (PE) PE 1: Capital Cost Estimation: Heat Exchanger PE 2: Operating Cost Estimation: Pump PE 3: Simple Process Comparison: Ethylene Oxide Manufacture, Air vs. Oxygen PE 4: Economic Equipment Selection: Pumps PE 5: Economic Process Selection: Heat Exchange
Short-Cut Equipment Design Methods (SCD) SCD 1: Pump Specification SCD 2: Compressor Specification SCD 3: Heat Exchanger Sizing SCD 4: Distillation Column Sizing SCD 5: Liquid-Vapor Separator Design SCD 6: Storage Tank Design
The Overall Process Plant (OPP) OPP 1: Steam Distribution OPP 2: Cooling Tower Operation OPP 3: Maximum Flare System Capacity OPP 4: Heat Exchanger Networks OPP 5: Storage Requirements for a Chemical Plant
Process Control (PC) PC 1: Instrument Accuracy and Precision: Flow Measurement PC 2: Temperature Measurement: Use as Indirect Composition Measurement PC 3: Trip and Alarm Logic PC 4: Control Stability: Heat Exchanger
Process Hazards (PH) PH 1: Estimating Air missions: Tank Filling PH 2: Estimating Effect of Worst-Case Explosion PH 3: Estimating Energy of an Explosion from Damage Assessment PH 4: Fire Water Requirements to Cool a Tank PH 5: Maintenance Problem: Purging a Vessel to Permit Entry
Process Reliability and Safety (PRS) PRS 1: Fault Tree Analysis: Constructing a Fault Tree for Rupture of a Reactor PRS 2: Fault Tree Analysis: Calculating Overall Event Probability PRS 3: HAZOP Applied to a Tank Car Loading Facility
Solutions to Problems
Appendix: SI Units and Conversion Factors References Index
Copyright © 1999, ETS Incorporated
|