作者: Łukasz Tomków , Maciej Cholewiński
DOI: 10.1016/J.ENCONMAN.2019.112178
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摘要: Abstract Utilization of the cold exergy regasified liquid natural gas (LNG) improves overall efficiency product chain by regaining part energy used to liquefy (NG). The application a standard organic Rankine cycle in case high-pressure LNG (complying with requirements delivery networks after regasification) leads comparatively low power generation and large loss exergy. In this paper we proposed novel multi-stage power-generating using binary working fluid. By separation ethane-krypton mixture into several streams different component ratios mass flows it was possible adjust process parameters increase net that can be produced per unit destroyed Furthermore, proper selection allowed heat capacity increased at any temperature region exchanger, thus efficiency. Factors affecting thermodynamic behavior system were presented analyzed numerical simulations. A significant total exergetic (from 10% 19.3%) observed when compared previously reported results for similar operating conditions. more than 15.4 kWh/t NG network pressure (8.5 MPa) obtained.