TY - GEN
T1 - EXPLORING the ENERGY and EXERGY PERFORMANCE of AN INTEGRATED HEAT RECOVERY SYSTEM in ALUMINUM SMELTERS USING A PARALLEL TWO-STAGE ORGANIC RANKINE CYCLE
AU - Abdelsamie, Mostafa
AU - Hassan Ali, Mohamed I.
N1 - Publisher Copyright:
© 2024 by ASME.
PY - 2024
Y1 - 2024
N2 - The primary aluminum industry stands out as one of the most energy-consuming and occasionally inefficient sectors, with approximately 50% of energy lost as waste heat. The challenge lies in the multitude of heat sources in aluminum smelters, each varying in quantity and temperature levels. Addressing this, the study employs the Parallel Two-stage Organic Rankine Cycle (PTORC) to integrate wasted heat from cathode sidewalls and exhaust gases into a unified recovery system. Based on a series of simulations, the current analysis delves into the impact of primary and secondary evaporation temperatures, as well as the number of integrated aluminum pots, on the energy and exergy performance of PTORC. Under specific design conditions, the results reveal that optimizing the system occurs when the primary evaporation temperature decreases and the secondary evaporation temperature increases. This leads to a substantial enhancement in both output power and thermal efficiency, accompanied by a reduction in exergetic destruction. At a primary evaporation temperature of 111.5°C and a secondary evaporation temperature of 78.5°C, the net output power reaches an optimal value of 3,840 kW. However, despite the increase in generated power, the exergy destruction of the recovery system experiences a notable rise with the number of integrated cells.
AB - The primary aluminum industry stands out as one of the most energy-consuming and occasionally inefficient sectors, with approximately 50% of energy lost as waste heat. The challenge lies in the multitude of heat sources in aluminum smelters, each varying in quantity and temperature levels. Addressing this, the study employs the Parallel Two-stage Organic Rankine Cycle (PTORC) to integrate wasted heat from cathode sidewalls and exhaust gases into a unified recovery system. Based on a series of simulations, the current analysis delves into the impact of primary and secondary evaporation temperatures, as well as the number of integrated aluminum pots, on the energy and exergy performance of PTORC. Under specific design conditions, the results reveal that optimizing the system occurs when the primary evaporation temperature decreases and the secondary evaporation temperature increases. This leads to a substantial enhancement in both output power and thermal efficiency, accompanied by a reduction in exergetic destruction. At a primary evaporation temperature of 111.5°C and a secondary evaporation temperature of 78.5°C, the net output power reaches an optimal value of 3,840 kW. However, despite the increase in generated power, the exergy destruction of the recovery system experiences a notable rise with the number of integrated cells.
KW - Aluminum industry
KW - organic Rankine cycle
KW - thermodynamic analysis
KW - waste heat recovery
UR - https://www.scopus.com/pages/publications/85204913364
U2 - 10.1115/HT2024-131608
DO - 10.1115/HT2024-131608
M3 - Conference contribution
AN - SCOPUS:85204913364
T3 - Proceedings of ASME 2024 Heat Transfer Summer Conference, HT 2024
BT - Proceedings of ASME 2024 Heat Transfer Summer Conference, HT 2024
T2 - ASME 2024 Heat Transfer Summer Conference, HT2024 collocated with the ASME 2024 Fluids Engineering Division Summer Meeting and the ASME 2024 18th International Conference on Energy Sustainability
Y2 - 15 July 2024 through 17 July 2024
ER -