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« Category overview | Thermal after-burning - TNV
Thermal post combustion, used - SOLD OUT(Article number: 2335)
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Memo Inquiry |
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Manufacturer: | Deutsche Fabrikat | ||||||
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Type: | Thermische Abluftreinigung | ||||||
Year of construction: | 1988 | ||||||
Description: | Manufacturer: German producer Type: Thermal exhaust air purification Year of construction: 1988 Interpretation of data Exhaust air volume flow rate: max. 496 m³ at 35 °C Exhaust air volume flow rate: min. 200 m³ Exhaust air temperature: approx. 35 °C (10 to 100 °C) Combustion air quantity: approx. 2600 m³ / s Combustion chamber temperature: approx. 760 °C max. 1000 °C Duration time of the combustion gases in the oxidation zone: min. 0.7 sec. at 760 °C Exhaust gas temperature after thermal oil heaters: approx. 280 °C Exhaust gas temperature after feedwater: about 195 °C max. pollutant concentration: 300 g / m³ Additional fuel: natural gas Hu = 8800 kcal / m³ Fuel requirement: approx. 80 Nm ³ / h when starting with fresh air Combustion chamber Thermal oil heating: 230/270 °C Thermal oil throughput: 25 m³ / h Heating capacity: approx. 595 kW Heat exchanger for preheating feed water Heating capacity: approx. 101 kW Exhaust gas cooling: approx 280/195 ° C Feedwater heating: 102/183 ° C Feed water flow rate: approx. 1070 kg / h Pressure loss exhaust side: approx. 3 mbar Heat exchanger for the generation of saturated steam Steam production: approx. 1070 kg / h Steam working pressure: 10 bar Permitted working pressure: 16 bar Feed water temperature: approx. 183 ° C Heat exchanger for preheating of fresh air Heating capacity: approx. 18 kW Air heating: approx. -10 / 95 ° C Air flow: max. approx. 450 m³ / h Pressure drop on the air side: approx. 3 mm WS Heating with low pressure hot water: 110/90 °C Lying countercurrent apparatus for heating by low pressure hot water Heating medium: high-pressure steam: approx 10 bar Power: approx. 18 kW Hot Water Heating: 90/110 °C Hot water flow rate: 0.8 m³ / h |
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Quantity: | 1 Pcs. | ||||||
Data in accordance with manufacturer | |||||||