Also options to copy and paste results as well as print preview and printing rtf file format for word processing to open in ms word and similar packages. + Export results to ms excel generated data sheet for editing. + Generate Results and export it to Shell & Tube Engineering Data sheet that can be also saved as a. + Save, Load and generate result in different formats
+ Support S.I Units and English (U.S) Units of measurement (249KB)Ĭase 11 - Industrial case - Retrofit Carpet Manufacturing Plant (145KB)Ĭase 12 - CHP and Heat Pumps versus Integrated Distillation Sequences (1027KB)Ĭase 13 - Example from Ahmad, Zamora, Bogataj, Rev&Fonio,Serna et al2015_06_06 (146KB)Ĭase 14 - Example with Multiple Utilities (196KB)Ĭase 15 - An improved tick-off procedure (the 9SP Aromatics Plant revisited) (286KB)Ĭase 16 - The importance of driving forces in heat exchanger network design (242KB)Ĭase 17 - A new benchmark for the 10SP1 literature case (311KB)Ĭase 18 - New benchmarks for the 10 streams literature case from Ahmad (1985) (482KB)Ĭase 19 - Example from Ahmad, Data set small 2015_06_08 (338KB)Ĭase 21 - Synthesis of heat exchanger networks - Smart Optimisation Procedures (245KB)Ĭase 22 - Pinch analysis with crisscross optimisation prior to design (282KB)Ĭase 23 - Benchmark Solutions for the Bandar Imam Aromatics Plant (290KB)Ĭase 24 - Benchmark Solutions for a Crude Fractionation Unit (691KB)Ĭase 25 - The Importance of Targeting in Heat Exchanger Network Synthesis (312KB)Ĭase26-thepowerofcrisscrossoptimisationpriortodesignforheatexchangernetworksynthesis.+ Step by step design and rating calculations.
The pinch analysis introduction package "Heatit - Basic" is available free of charge.Įxample studies marked as can be downloaded without any restriction, provided you are so kind to identify yourself to the author.Ĭase 1 Pinch analysis with crisscross optimisation - The principle (195KB)Ĭase 2 - Example from Gundersen and Grossmann 2016_03_08 (295KB)Ĭase 3 - Example from Colberg and Morari (475KB)Ĭase 4 - Example from Linnhoff & Ahmad - The 9SP Aromatics Plant 2013_10_05 (398KB)Ĭase 5 - Example from Björk and Pettersson (159KB)Ĭase 6 - Example from the Magnets User Manual (292KB)Ĭase 7 - Synthesis of Heat Exchanger Networks with Equal Heat Transfer Coefficients (159KB)Ĭase 8 - Example from Shenoy modified by Frauso-Hernandez (94KB)Ĭase 10 - Example from WU Xiao et al. There is no such thing like an optimum DTMin or Heat Recovery Approach Temperature HRAT nor any Exchanger Minimum Approach Temperature EMAT to be considered there only is optimum integration combined with optimised crisscross. Crisscross optimisation prior to design is an excellent tool to generate such data set.
Heat exchanger network synthesis can be facilitated by using an optimised data set for the initial design.
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