Wilcox
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× MATLAB × Data Analysis
Chemical
engineering equipment types, descriptions, design, selection
This color indicates a
link available via Clarkson University (off-campus
access)
See
also Safety
considerations in design, separation techniques
and HYSYS.
General sources of information
·
From
Walas (Rules of Thumb in the Front Matter of Walas); (Same
via AIChE student member site)
·
Rules of Thumb for Chemical Engineers, 2nd edition,
Carl Branan (1998) Gulf Publishing Company: 660 R935
Clarkson Library.
·
ChEResources Updated online.
·
Applied Process Design for Chemical and Petrochemical
Plants (Ch 0)
·
HVAC
·
Appendix E in “Plant Design and Economics for Chemical Engineers,”
5th edition, by M.S. Peters, K.D. Timmerhaus
and R.E. West (McGraw-Hill, NY, 2003).
·
Appendix C in “Chemical Engineering Process Design and Economics:
A Practical Guide,” 2nd edition, by G.D. Ulrich and P.T. Vasudevan (Process Publishing, Durham, N.H., 2004)
·
Perry's
Chemical Engineers’ Handbook, 8th edition
·
Marks’
Standard Handbook for Mechanical Engineers, 11th Edition
·
Chemical
Process and Design Handbook
·
Handbook
of Chemical Engineering Calculations, 3rd Edition
·
Handbook
of Environmental Engineering Calculations, 2nd Edition
·
Handbook
of Petroleum Refining Processes, Third Edition
·
Heat
Transfer in Process Engineering
·
Working
Guide to Process Equipment, 3rd Edition
·
Chemical
Reactor Design, Optimization and Scaleup
HYSYS and UniSim
:
Note
that the equipment palette in shows only some of the equipment that it can
model. Click on Flowsheet, Add Operation (or press F12) to see a complete
list, part of which is shown at HYSYS/UniSim.
Distillation,
absorption, stripping columns
Pressure changes,
pumps, compressors and piping systems
Vessels
·
Sizing of flash
drums, surge tanks and accumulators
Liquid-liquid extraction
Use LLE heuristics to
size equipment. See also Perry's chapter 15, particularly equations 15-65 and
15-66. The delta P for a LLE column is
approximately the weight of the two phases in the column per cross-sectional
area. Note that the pressure drop is not
nearly as important for LLE as for distillation because liquid-liquid
equilibria are not sensitive to pressure.
Instrumentation and control
Bioprocessing
Miscellaneous
Clarkson's Department of Chemical and
Biomolecular Engineering
Disclaimer: The
material on these pages is intended for instructional purposes by Clarkson
University students only. Neither
Clarkson University nor Professor Wilcox are responsible for problems caused by
using this information.
Last updated October
11, 2011. Comments and corrections
should be sent to Professor
William R. Wilcox
Wilcox
home × ChE design home × Professional × General × Properties × Equipment × Separation × HYSYS &
UniSim × Costs × Safety × Case studies × Excel
× MATLAB × Data Analysis