The present study aims to conduct a thermodynamic analysis of a novel concept that synergistically integrates clean hydrogen and power production with a liquefied natural gas (LNG) regasification system. The designed integrated energy system aims to achieve hydrogen production, power production, LNG regasification, carbon capture, storage, and in situ recirculation. Hydrogen sulfide (H2S) from industrial waste streams is used as a major feedstock, and a specific combustion of H2S is employed as a hydrogen production method. CO2 obtained from the combustion process is liquefied and pumped at a high pressure to be recirculated back into the power generation combustion process. The entire plant is simulated in the Aspen Plus simulation environment, and a comprehensive thermodynamic assessment including the energy and exergy analysis is conducted. Additionally, several parametric studies are conducted to identify suitable operating parameters. From the sensitivity analyses, it is found that at 20 % CO2 recirculation, the hydrogen production rate decreases by 48.27 % when the operating pressure is increased from 0.05 bar to 3 bar. The adiabatic temperature is reduced by 56.86 %, 52.26 %, and 49.45 %, when 50 %, 60 %, and 70 % CO2 is recirculated in the oxidant stream atan oxygen to natural gas (ONG) ratio of 0.5. The energy and exergy efficiencies of the system are found to be 71.48 % and 60.69 %, respectively. The present system avoids 2571.94 tons/yr of CO2 emissions for clean hydrogen production and 1426.27 tons/yr of CO2 for clean power production which would otherwise be emitted from steam methane reforming and coal gasification.
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