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      "pump_entropy_rise_J_kgK": 12.011575821474707,
      "expander_entropy_rise_J_kgK": 347.74694924553387,
      "first_heater_entropy_generation_at_300K_J_kgK": 1682.692331571017,
      "second_heater_entropy_generation_at_330K_J_kgK": 331.9175125993152,
      "efficiencies_assumed": {
        "pump": 0.65,
        "expander": 0.65,
        "generator": 0.92,
        "pump_motor": 0.9
      },
      "max_fluid_mass_kg_from_first_heat_envelope": 9.119755487561964,
      "max_fluid_mass_kg_from_existing_loss_heat_plus_new_loss_recovery": 2.0165277075068486,
      "allocated_N2_mass_kg": 2.0,
      "gross_net_DC_before_unallocated_auxiliaries_J": 122504.288703396
    },
    {
      "pressure_bar": 15.0,
      "expander_inlet_K": 240.0,
      "liquid_initial_K": 77.3549939095929,
      "pumped_liquid_K": 78.18658338774205,
      "expander_outlet_K": 153.74210152698942,
      "terminal_cooling_exit_K": 263.15,
      "inlet_phase": "supercritical_gas",
      "outlet_phase": "supercritical_gas",
      "thermodynamic_state_gate_passed": true,
      "pump_shaft_J_kg": 2669.4566125274832,
      "pump_DC_J_kg": 2966.0629028083144,
      "expander_shaft_J_kg": 85209.72421385148,
      "generator_DC_J_kg": 78392.94627674337,
      "net_DC_before_unallocated_auxiliaries_J_kg": 75426.88337393505,
      "first_heat_input_J_kg": 363200.5781281293,
      "second_cooling_heat_input_J_kg": 114176.28651124443,
      "new_conversion_loss_heat_J_kg": 7113.384227388944,
      "minimum_temperature_approach_K": 60.0,
      "fluid_first_law_residual_J_kg": 0.0,
      "initial_cold_fluid_availability_J_kg": 741686.2090306964,
      "terminal_fluid_availability_J_kg": 1716.8385661141583,
      "exergy_balance_residual_J_kg": -1.1641532182693481e-10,
      "pump_entropy_rise_J_kgK": 12.011575821474707,
      "expander_entropy_rise_J_kgK": 351.01699822061437,
      "first_heater_entropy_generation_at_300K_J_kgK": 1736.3617020853974,
      "second_heater_entropy_generation_at_330K_J_kgK": 215.02851308488346,
      "efficiencies_assumed": {
        "pump": 0.65,
        "expander": 0.65,
        "generator": 0.92,
        "pump_motor": 0.9
      },
      "max_fluid_mass_kg_from_first_heat_envelope": 8.020958177462106,
      "max_fluid_mass_kg_from_existing_loss_heat_plus_new_loss_recovery": 2.5737723825311547,
      "allocated_N2_mass_kg": 2.0,
      "gross_net_DC_before_unallocated_auxiliaries_J": 150853.7667478701
    }
  ],
  "selected": {
    "pressure_bar": 10.0,
    "expander_inlet_K": 200.0,
    "liquid_initial_K": 77.3549939095929,
    "pumped_liquid_K": 77.88905197393791,
    "expander_outlet_K": 135.36273194070657,
    "terminal_cooling_exit_K": 263.15,
    "inlet_phase": "supercritical_gas",
    "outlet_phase": "supercritical_gas",
    "thermodynamic_state_gate_passed": true,
    "pump_shaft_J_kg": 1715.1760925612714,
    "pump_DC_J_kg": 1905.751213956968,
    "expander_shaft_J_kg": 63227.36973108003,
    "generator_DC_J_kg": 58169.180152593624,
    "net_DC_before_unallocated_auxiliaries_J_kg": 56263.42893863666,
    "first_heat_input_J_kg": 322880.02381570346,
    "second_cooling_heat_input_J_kg": 133468.76686086503,
    "new_conversion_loss_heat_J_kg": 5248.764699882099,
    "minimum_temperature_approach_K": 66.85000000000002,
    "fluid_first_law_residual_J_kg": 5.820766091346741e-11,
    "initial_cold_fluid_availability_J_kg": 741686.2090306964,
    "terminal_fluid_availability_J_kg": 1716.8385661141583,
    "exergy_balance_residual_J_kg": 0.0,
    "pump_entropy_rise_J_kgK": 7.73290062432261,
    "expander_entropy_rise_J_kgK": 287.274542062235,
    "first_heater_entropy_generation_at_300K_J_kgK": 1805.1357034885173,
    "second_heater_entropy_generation_at_330K_J_kgK": 290.2154290798641,
    "efficiencies_assumed": {
      "pump": 0.65,
      "expander": 0.65,
      "generator": 0.92,
      "pump_motor": 0.9
    },
    "max_fluid_mass_kg_from_first_heat_envelope": 9.022597969264945,
    "max_fluid_mass_kg_from_existing_loss_heat_plus_new_loss_recovery": 2.149083890560641,
    "allocated_N2_mass_kg": 2.0,
    "gross_net_DC_before_unallocated_auxiliaries_J": 112526.85787727332
  },
  "source": "https://coolprop.org/fluid_properties/fluids/Nitrogen.html",
  "physical_interpretation": "Finite cold-store and pressure/heat conversion opportunity. Liquid production/recharge, heat exchangers and unallocated auxiliaries are not free. This is not energy created by a vacuum.",
  "resource_basis": {
    "first_heat_envelope_J": 2913216.647195783,
    "existing_electrical_path_loss_heat_J": 275555.54109181894,
    "time_reference_s": 8.28,
    "first_heat_envelope_is_a_requirement_screen_not_measured_UA": true
  },
  "vehicle_energy_credit_J": 0.0,
  "limits": [
    "No driving result receives this electrical output. Pump, expander, storage, heat exchanger, flow pressure loss and additional mass are not yet integrated into the four-wheel vehicle.",
    "The 2 kg cap is a finite proposed inventory, not an optimised or installed tank. Containment and hardware mass are excluded from this standalone thermodynamic screen.",
    "First heating uses a specified 300-to-280 K heat-source envelope; the real transient air-to-nitrogen exchanger has not been designed or measured.",
    "Second cooling is limited by the earlier calculated electrical conversion heat, plus the new generator/pump conversion losses counted exactly once.",
    "Auxiliary circulation, valves, control, boil-off, temperature approaches under real flow and nitrogen liquefaction/recharge energy must still be measured or allocated. Net useful vehicle benefit is unestablished.",
    "Pressure and cryogenic states are analysis points, not fabrication instructions."
  ]
}
