Heat, TNV-7.500, 2019, 800 kW, 75000 Nm3/hr Exhaust Air Volume, Zeolite Rotor System

Description

  1. Overview
    1. Type: Thermal oxidizer
    2. Brand: Heat
    3. Model: TNV-7.500
    4. Year: 2019
    5. Unused Heat Austria TNV-7.500 thermal oxidizer
    6. A zeolite rotor system and thermal oxidizer with recuperative heat exchanger
    7. Max. burner power: 800 kW -- 45,500 btu/min
  2. Main Technical Data
    1. Exhaust air volume: max. 75,000 nm3/hr
    2. Exhaust air temperature: 20-35°C / 68-95°F
    3. Dust content: <1.0 mg/m3, 800 (max. 1,100) mg/nm
    4. Pollutants (main constituents): 75% xilol, 25% other solvents
    5. Additional fuel: Natural gas
    6. Pre pressure additional fuel: 100 mbar / 1.45 psi
    7. Calorific value additional fuel: 38,600 kj/mn3 / 1,036 btu/scf
    8. Burner supply power: 700 kW
    9. Time in combustion chamber: 1 s
    10. Combustion chamber temp.: 750°C (max. 800°C) / 1,382°F (max. 1,472°F)
  3. General Information
    1. A zeolite rotor with RCO is an industrial air pollution control system that uses a zeolite rotor concentrator to capture and concentrate volatile organic compounds (VOCs) from large air volumes, which are then fed into a regenerative catalytic oxidizer (RCO) to be destroyed.
    2. This combined system is highly effective for treating large, low-concentration air flows, as the rotor significantly reduces the air volume and increases the VOC concentration, making the oxidation process in the RCO more fuel-efficient.
  4. Technical Details
    1. Desorption Air Exhaust Heat Exchanger HE 1
      1. Desorption air volume: 7,500 nm³/h
      2. Desorption air temperature before HE: 60°C (140°F)
      3. Desorption air temperature after HE: 500°C (932°F)
      4. Clean air volume: 7,500 nm³/h
      5. Clean air temperature before HE: 750°C (1,382°F)
      6. Clean air temperature after HE: 330°C (626°F)
      7. Exchanged amount of heat: 1,230 kW
    2. Cooling Air – Exhaust Air Heat Exchanger HE 2
      1. Quantity of cooling air: 7,500 nm³/h
      2. Cooling air temperature before HE: 100°C (212°F)
      3. Cooling air temperature after HE: 200°C (392°F)
      4. Exhaust gas volume: 7,500 nm³/h
      5. Exhaust gas temperature before HE: 330°C (626°F)
      6. Exhaust gas temperature after HE: 235°C (455°F)
      7. Exchanged amount of heat: 270 kW
    3. Exhaust Gas – Hot Water Heat Exchanger HE 3
      1. Exhaust gas volume: 7,500 nm³/h
      2. Exhaust gas temperature before HE: Ø 250°C (482°F)
      3. Exhaust gas temperature after HE: 115°C (239°F)
      4. Secondary medium: Warm water with 30% glycol percentage
      5. Throughput: 31 m³/h
      6. Temperature before HE (secondary medium): 90°C (194°F)
      7. Temperature after HE (secondary medium): 110°C (230°F)
      8. Exchanged amount of heat: Ø 370 kW (max. 650 kW)
    4. Exhaust Air – Fresh Air Heat Exchanger HE 4
      1. Exhaust air volume: 75,000 nm³/h
      2. Exhaust air temperature before HE: 25°C (77°F)
      3. Exhaust air temperature after HE: -3°C (26°F)
      4. Amount of fresh air: 75,000 nm³/h
      5. Fresh air temperature before HE: -15°C (5°F)
      6. Fresh air temperature after HE: +15°C (59°F)
      7. Exchanged amount of heat: 750 kW
  5. Exhaust Gas and Clean Air Values
    1. Organic C – concentration after concentrator: max. 50 mg/nm³
    2. Organic C – concentration after RTO burner: max. 20 mg/nm³
    3. CO – concentration after RTO burner: max. 100 mg/nm³
    4. NOx – concentration after RTO burner: max. 100 mg/nm³
    5. Measured values as ½ hour average values based on actual measured oxygen content.
  6. Resources
    1. Electric power: 3x480V, 60Hz + PE + N
    2. Rated power supply: 155 kW
    3. Natural gas: Hu = 38,600 kj/nm³
    4. Natural gas - pre pressure: Pe = 100 mbar flow pressure /// Pe = 1.45 psi flow pressure
    5. Natural gas - connected load: 85.0 nm³/h
    6. Compressed air: Oil-free /// dry
    7. Compressed air - pre pressure: min. 6.0 bar(g) /// min. 87 psi(g)
    8. Compressed air - connected load: 1.0 nm³/h
  7. Resource Consumption
    1. Natural Gas
      1. At 75,000 nm³/h exhaust air without pollutant content: 75 nm³/h
      2. At 75,000 nm³/h exhaust air with 800 mg/nm³ solvent: 15 nm³/h
    2. Compressed Air
      1. Compressed air consumption for cooling UV probe: 1.0 nm³/h
      2. Compressed air consumption for emergency cooling concentrator: 100.0 nm³/h
    3. Electric Power
      1. Without heat recovery (HE4): 120.0 kWh
      2. With heat recovery (HE4): 150.0 kWh