Benha University

محمد أشرف محمد

مدرس مساعد

كلية الهندسة ببنها الهندسة الميكانيكية

Techno evaluation of an advanced standalone system based on waste heat recovery for power, fresh water, hydrogen, and cooling

International Communications in Heat and Mass Transfer • 2026
العودة
معلومات البحث
المؤلفون Mahmoud, M. A.Nada, SamehHassan, Hamdy
الكلمات المفتاحية Adsorption cooling; Humidification-dehumidification; Organic Rankine Cycle; PEM electrolyzer; Polygeneration system; Waste heat recovery
المجلة العلمية International Communications in Heat and Mass Transfer
الناشر Elsevier Ltd
المجلد 172
العدد P6
الصفحات 110682
publication.type International
رابط البحث Open Link
المواد المرفقة Not Available
الملخص
This study evaluates a new standalone polygeneration system designed to convert waste-heat steam into electricity, green hydrogen, freshwater, and cooling via an integrated Organic Rankine Cycle (ORC), Proton Exchange Membrane (PEM) electrolyzer, Humidification–Dehumidification (HDH) desalination unit, and Adsorption Cooling System (ACS). The thermodynamic performance of the integrated system is modeled and analyzed under varying waste steam qualities (0.05–0.97) and heat allocation ratios using MATLAB® simulations. Results indicate that increasing the inlet steam quality from 0.05 to 0.97 linearly scales the ORC net power output from 72.65 kW to 929.66 kW, driving the PEM electrolyzer to produce hydrogen at rates ranging from 1.79 kg/h to 20.70 kg/h, respectively. The residual heat is recovered to drive the bottoming cycles; an optimal allocation strategy (95% heat to HDH at 7 kg/s saline flow) achieved a peak freshwater yield of 901.2 kg/h (GOR = 1.12). Conversely, balanced configurations (20% HDH / 80% ACS) maximized the bottoming cycle synergy, delivering 17.98 kW of cooling (COP = 0.506). A critical thermodynamic trade-off is observed regarding the overall Energy Utilization Factor (EUF); while high steam qualities maximize hydrogen yield, the EUF declines to approximately 4.4% due to high latent heat consumption. However, optimizing the configuration for low-quality steam (Configuration 9) achieved a peak EUF of 46.87% by maximizing freshwater recovery. The study concludes that adaptive heat allocation is essential to balance the trade-off between high-value hydrogen production and overall thermal energy utilization.
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