{
  "source_ids": [
    "MWS01"
  ],
  "source_pdf_sha256": "76c7d9cf91c11be2d4b95449645642e8cc914bb23632cf6b523d7dbf0761ade8",
  "data": {
    "conditions": {
      "source_id": "MWS01",
      "locators": [
        "PDF p.2 / printed 1832, §§2.1–2.2",
        "PDF p.3 / 1833, §2.2 and Figs 1–2",
        "PDF p.4 / 1834, Eqs 3–4, §2.3 and Table 1"
      ],
      "feedstock": {
        "type": "ground waste truck tyre",
        "supplier": "Eco Power Synergy Sdn Bhd",
        "tyre_brand": null,
        "size_mm": [
          5,
          10
        ],
        "tyre_charge_g": 100,
        "steel": "removed by magnetic separation",
        "textile_cord_status": "not reported",
        "tyre_drying_before_reactor": "not clearly reported; 105 °C redrying is described for analyses, not necessarily for reactor feed"
      },
      "added_absorber": {
        "material": "granular activated carbon",
        "size_mm": [
          5,
          10
        ],
        "charge_g": 100,
        "mass_ratio_absorber_to_tyre": 1,
        "pretreatment": {
          "temperature_C": 110,
          "duration_h": 12,
          "device": "ventilated oven"
        },
        "mixture": "homogeneously mixed",
        "reuse_cycles_reported": false,
        "fresh_surface_area_m2_g": 1202.34,
        "used_surface_area_m2_g": 416.49,
        "surface_area_locator": "p.6 / 1836, §3.2.2 and Fig.5"
      },
      "reactor": {
        "mode": "batch",
        "vessel": "cylindrical quartz glass reactor with three-neck cover",
        "capacity_dimensions": "not reported in main article",
        "equipment": "modified multimode digital microwave",
        "frequency_GHz": 2.45,
        "nominal_power_W": 1000,
        "calibrated_output_power_W_reported": 695,
        "reported_calibration_efficiency_percent": 69.5,
        "calibration_method": "referenced oven cooking-efficiency standard, ref.23; per-level details cited as Fig.S1",
        "absorbed_power_in_tyre_W": null,
        "metered_wall_electricity_kWh": null,
        "rated_vs_wall_input_boundary": "1000 W is not demonstrated to be wall-plug electrical demand; 695 W is calibrated output, not demonstrated absorption by tyre+AC",
        "calibration_fit_fig2": {
          "slope": 0.7117,
          "intercept_W": -53.044,
          "R2": 0.9889,
          "fit_at_1000_W": 658.656,
          "interpretation": "fit value differs from 695 W point; this is not by itself proof of contradiction because regression residuals are possible"
        }
      },
      "temperature": {
        "setpoints_C": [
          300,
          400,
          450,
          500,
          550,
          600
        ],
        "measurement": "ceramic-coated R-type thermocouple in middle of tyre/AC bed; real-time acquisition",
        "point_reading_not_temperature_field": true,
        "raw_profiles_supplied": false,
        "control_algorithm_duty_cycle": "not reported",
        "heating_rate_C_min": null
      },
      "atmosphere": {
        "gas": "N2",
        "flow_mL_min": 300,
        "pressure": "not quantified",
        "initial_purge_time_min": null
      },
      "time": {
        "hold_at_set_temperature_h": 1,
        "heatup_time_min": null,
        "microwave_on_time_min": null,
        "source_also_states_maximum_power_selected": true,
        "interpretation": "one-hour hold does not prove one hour of uninterrupted 695 W output, nor total batch duration"
      },
      "condensation": {
        "equipment": "glass condensers, water-bath chiller, oil collectors",
        "coolant_temperature_literal": "±5 °C",
        "coolant_temperature_ambiguity": "source prints ±5 °C without an unambiguous target/reference",
        "separate_oil_water_layers": true,
        "oil_workup": "dissolved in pre-weighed dichloromethane",
        "solvent_removal_and_oil_mass_correction_protocol": "not adequately described",
        "wax_separately_measured": false
      },
      "balances": {
        "oil": "oil mass / feedstock mass × 100",
        "char": "char mass / feedstock mass × 100",
        "gas": "100 − (oil yield + char yield); by difference, not measured gas mass",
        "oil_water_split_quantified": false,
        "AC_subtraction_from_solid_and_mass_denominator": "not explicitly described; do not silently interpret char as independently weighed tyre-derived char or denominator as the 200 g total mixture",
        "independent_mass_closure": false,
        "replication_number": "not stated; Fig.4 has error bars but their basis is not specified"
      },
      "energy_boundary": {
        "specific_electricity_kWh_kg_tyre": null,
        "specific_electricity_kWh_kg_oil": null,
        "oil_energy_recovery": "oil yield × HHV_oil/HHV_tyre; product energy recovery, not electrical process efficiency",
        "auxiliaries_unmetered": [
          "AC drying 110 °C for 12 h",
          "stirrer",
          "chiller and circulation",
          "N2 provision",
          "sample and condensate handling"
        ],
        "safe_conclusion": "No measured net energy benefit against conventional heating is established."
      }
    },
    "feedstock_table1": {
      "source_id": "MWS01",
      "locator": "PDF p.4 / 1834, Table 1",
      "proximate_wt_percent": {
        "moisture": 0.92,
        "volatile_matter": 65.35,
        "fixed_carbon": 29.53,
        "ash_at_900_C": 4.2
      },
      "ultimate_dry_wt_percent": {
        "C": 80.33,
        "H": 7.66,
        "N": 0.35,
        "S": 0.87,
        "O_by_difference": 10.79
      },
      "HHV_MJ_kg": 39.87,
      "LHV_MJ_kg": 38.14,
      "conflict": "§3.1 prose gives ash 4.02; Table 1 gives 4.20. Table numbers sum to 100.00; preserve the conflict."
    },
    "oil_quality_table4": {
      "source_id": "MWS01",
      "sample": "TTPO500",
      "locator": "PDF p.10 / 1840, Table 4",
      "elemental_wt_percent": {
        "C": 87.75,
        "H": 10.63,
        "N": 0.6,
        "S": 0.67,
        "O_by_difference": 0.35
      },
      "kinematic_viscosity_at_40_C": {
        "value": 3.53,
        "unit": "not printed in Table 4; do not silently supply cSt"
      },
      "density_at_15_C_kg_L": 0.9,
      "flash_point_C": "<30",
      "water_content_percent": 0.47,
      "water_basis": "Table 4 says %, not explicitly mass/volume; method is Karl Fischer",
      "HHV_MJ_kg": 42.39,
      "LHV_MJ_kg": 40.12,
      "GC_table": "cards/MW01/numeric/table3_gc_relative.csv",
      "GC_basis": "relative chromatographic content; Fig.7 explicitly labels Area [%]. Not calibrated wt% of oil or yield on tyre.",
      "limonene_relative_percent_by_T": {
        "300": 9.29,
        "400": 14.29,
        "450": 11.37,
        "500": 6.02,
        "550": 5.33,
        "600": 5.29
      },
      "diesel_comparison": "commercial diesel values in Table 4 are literature comparators, not a conventional-pyrolysis control",
      "qualified_product": "crude pyrolysis liquid needing further upgrading; not established drop-in diesel fuel"
    }
  }
}
