Design of heat exchanger network physical layout in process plants using a mixed-integer model
Author:
Funder
CNPq
Publisher
Springer Science and Business Media LLC
Link
https://link.springer.com/content/pdf/10.1007/s43153-024-00462-y.pdf
Reference32 articles.
1. Akbarnia M, Amidpour M, Shadaram A (2009) A new approach in pinch technology considering piping costs in total cost targeting for heat exchanger network. Chem Eng Res Des 87(3):357–365. https://doi.org/10.1021/ie010343l
2. Aldridge GA, Verykios XE, Mutharasan R (1984) Recovery of ethanol from fermentation broths by catalytic conversion to gasoline. 2. Energy analysis. Ind Eng Chem Process Des Dev 23:733–737. https://doi.org/10.1021/i200027a018
3. Backhurst JR, Harker JH (1973) Process plant design. Butterworth-Heinemann, Oxford
4. Barker GB (2017) The engineer’s guide to plant layout and piping design for the oil and gas industries. Gulf Professional Publishing, Oxford
5. Bausbacher E, Hunt R (1993) Process plant layout and piping design. Prentice Hall PTR, Hoboken
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