heat exchangers index
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Wilcox home ChE design home Professional General Properties Equipment Separation HYSYS &
UniSim Costs Safety Case studies Excel MATLAB Data Analysis
Heat exchangersThis color indicates a link available via Clarkson University (off-campus
access)
General information Equations Thermodynamic models List of heating methods, temperatures, costs Design of plate and frame heat exchangers Predicting and accounting for heat exchanger fouling Water-steamAll properties, in tables, graphs, interactive tables, and
calculator.
Heuristics
For pressure drops, approach temperatures, utilities, refrigerants, etc. Heuristics
HVACSee section 21.01 for standard steam pressures. Table 9.11 inTurton et al. Rules of Thumb for Chemical Engineers, 2
ndedition, Carl Branan (1998)Gulf Publishing Company: 660 R935 Clarkson Library.
ChEResourcesUpdated online. Appendix E in Plant Designand Economics for Chemical Engineers,
5thedition, by M.S. Peters, K.D. Timmerhaus and R.E. West (McGraw-Hill,NY, 2003).
Appendix C in Chemical Engineering Process Design and Economics: APractical Guide, 2ndedition, by G.D. Ulrich andP.T. Vasudevan (Process Pubishing, Durham, N.H., 2004)
Access Engineering(McGraw-Hill books, available freeforAIChEmembers through their site)
Heat Transfer in Process Engineering
Perry's Chemical Engineers Handbook, 8th edition
Marks Standard Handbook for Mechanical Engineers, 11th Edition
Handbook of Chemical Engineering Calculations, 3rd Edition
Working Guide to Process Equipment, 3rd Edition
Typical heat transfer coefficients
WARNING: The values of U originating from Walas are extremelymisleading and confusing. They should not be used. (That is, theheuristics posted here, those in Turton et al., and those fromAIChE.) Use instead one of the following sources: Table 11-3 on p 11-25 of Perry's (free access throughAIChEfor members) Typical U values
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itionhttp://accessengineeringlibrary.com/browse/heat-transfer-in-process-engineeringhttp://www.aiche.org/resources/elibraryhttp://accessengineeringlibrary.com/http://www.cheresources.com/exprules.shtmlhttp://vig.prenhall.com/catalog/academic/product/0,1144,0130647926,00.htmlhttp://www.knovel.com/web/portal/basic_search/display?_EXT_KNOVEL_DISPLAY_bookid=2354http://www.clarkson.edu/~wilcox/Design/heurist.pdfhttp://www.knovel.com/knovel2/Toc.jsp?BookID=1251&VerticalID=0http://www.clarkson.edu/~wilcox/Design/hxfoul.pdfhttp://www.clarkson.edu/~wilcox/Design/hxdesign.pdfhttp://www.clarkson.edu/~wilcox/Design/heatmeth.dochttp://people.clarkson.edu/~wilcox/Design/thermodl.htmhttp://www.clarkson.edu/~wilcox/Design/hxequns.dochttp://people.clarkson.edu/~wwilcox/Design/OffCampusAccess.htmhttp://people.clarkson.edu/~wwilcox/Design/OffCampusAccess.htmhttp://people.clarkson.edu/~wwilcox/DoElinks.htmhttp://people.clarkson.edu/~wilcox/ES100/eqsolve.htmhttp://people.clarkson.edu/~wilcox/extut.htmhttp://people.clarkson.edu/~wilcox/Design/casestep.htmhttp://people.clarkson.edu/~wilcox/Design/refsafe.htmhttp://people.clarkson.edu/~wilcox/Design/refcosts.htmhttp://people.clarkson.edu/~wilcox/Design/refhysys.htmhttp://people.clarkson.edu/~wilcox/Design/refhysys.htmhttp://people.clarkson.edu/~wilcox/Design/refsepn.htmhttp://people.clarkson.edu/~wilcox/Design/refequip.htmhttp://people.clarkson.edu/~wilcox/Design/refchem.htmhttp://people.clarkson.edu/~wilcox/Design/refgen.htmhttp://people.clarkson.edu/~wilcox/Design/refprof.htmhttp://people.clarkson.edu/~wilcox/Design/refs.htmhttp://people.clarkson.edu/~wilcox/ 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Excellent nomograph: Figure 12.1 on p 799 ofChemical EngineeringDesign: Principles, Practice and Economics of Plant and ProcessDesign byGavin Towlerand Ray Sinnott
Comprehensive tables: Table 4-15, pp 206-209 in Chemical EngineeringProcess Design and Economics: A Practical Guide, 2ndedition, by G.D.
Ulrich and P.T. Vasudevan (Process Publishing, Durham, N.H., 2004).
Table 13.5 on p 431 of Product and Process Design Principles: Synthesis,Analysis, and Evaluation, 2ndedition, by W.D. Seider, J.D. Seader andD.R. Lewin(Wiley, NY, 2004).
Heat transfer fluids Knovel SteamTables Heat transfer liquidsfrom Perrys 5
thedition (right click and Save Target Asto download to your computer)
HITEC heat transfer salt Dow:High temperature liquids; Low temperature liquids Paratherm heat transfer fluids(Operating ranges for heating and cooling.)
Sasol heat transfer fluids(Operating ranges for heating and cooling.)
Therminol heat transfer fluids(Operating ranges for heating and cooling.) MultiTherm heat transfer fluids(Operating ranges for heating and cooling.)
Simulation usingHYSYS or UniSimIt is a very serious error to show a pressure increase for a streamgoing through a heat exchanger Refrigeration and heating fluidsbuilt into HYSYS and UniSim For the initialLevel-1 simulation,use heaters and coolers. To find the heat
exchanger areas and utility requirements needed for economic analysis,use the following methods:
Heat exchanger sizing using HYSYS or UniSim
Reboiler and condenser sizing using HYSYS or UniSim
Heat exchanger design using UniSimIf UniSimsHeat Exchangers is also installed along with UniSimDesign, then heat exchanger details can be calculated rather thanestimated. The following methods are available: Shell and tube exchangers can be designed in UniSim Design as
follows. Open a heat exchanger and click on Design/Parameters/HeatExchanger Model and select UniSim STE Engine.
The following types of heat exchangers can be designed using the HeatExchanger engine:
CFE: CrossFlow Exchanger
FPH: Fired Process Heater
FWH: FeedWater Heat exchanger PFE: Plate-Fin Exchanger PHE: Plate Heat Exchanger STE: Shell & Tube Exchanger
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Last revis ed September 15, 2012. Please email qu estions , comment s
and suggest ions toW.R. Wilco x
Disclaimer: The mater ial on these pages is intended fo r instruc t ional
purp oses by Clarkson Univers i ty students only. Nei ther Clarkson
Univers i ty nor Professor Wilcox are respon sib le for problems c aused by
us ing th is in formation.
Wilcox home ChE design home Professional General Properties Equipment Separation HYSYS &
UniSim Costs Safety Case studies Excel MATLAB Data Analysis
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