Combined Pinch and exergy numerical analysis for low temperature heat exchanger network

To reduce the dependence on fossil fuel, Process Integration and energy efficiency are crucial in chemical process industry to minimise the consumption of fossil fuels and electricity demand through Heat Exchanger Network (HEN). Pinch Analysis is well established to optimal HEN design to maximize th...

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Veröffentlicht in:	Energy (Oxford) 2018-06, Vol.153, p.100-112
Hauptverfasser:	Hamsani, Muhammad Nurheilmi, Walmsley, Timothy Gordon, Liew, Peng Yen, Wan Alwi, Sharifah Rafidah
Format:	Artikel
Sprache:	eng
Schlagworte:	Case studies Chemical process industries Compression Dependence Design Electric power demand Electricity consumption Energy conversion efficiency Energy efficiency Energy recovery Exergy Exergy analysis Fossil fuels Graphical representations Heat Heat exchanger network Heat exchangers Heat recovery Low temperature Mathematical models Numerical analysis Numerical methods Operating costs Organic chemistry Pinch analysis Process integration Refrigeration Temperature effects Temperature gradients Temperature requirements Thermodynamics
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