Advanced Combustion and Aerothermal Technologies: by Nick Syred, Artem Khalatov

By Nick Syred, Artem Khalatov

The NATO ARW complicated Combustion and Aerothermal applied sciences: Environmental safety and pollutants mark downs, was once held in Kiev, might 2006. The workshop was once Co-Directed via Profs. N. Syred and A.Khalatov, winners of the NATO medical Prize 2002, and used to be equipped by way of the Institute of Thermophysics (Ukraine) and Cardiff college, united kingdom. the first Workshop goals have been to evaluate the prevailing wisdom on complex combustion and aerothermal applied sciences supplying decreased environmental impression, to spot instructions for destiny study within the box, and to advertise the shut relationships and company contacts among scientists from NATO and companion international locations.

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By Nick Syred, Artem Khalatov

The NATO ARW complicated Combustion and Aerothermal applied sciences: Environmental safety and pollutants mark downs, was once held in Kiev, might 2006. The workshop was once Co-Directed via Profs. N. Syred and A.Khalatov, winners of the NATO medical Prize 2002, and used to be equipped by way of the Institute of Thermophysics (Ukraine) and Cardiff college, united kingdom. the first Workshop goals have been to evaluate the prevailing wisdom on complex combustion and aerothermal applied sciences supplying decreased environmental impression, to spot instructions for destiny study within the box, and to advertise the shut relationships and company contacts among scientists from NATO and companion international locations.

Show description

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Extra resources for Advanced Combustion and Aerothermal Technologies: Environmental Protection and Pollution Reductions

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B. USTIMENKO The heat loss with the effluent gases is determined from the effluent gas temperature (Tg), flow rate (G1), and composition obtained through the gas analysis. The measured temperature, pressure, and composition of gases are fed into the TERRA code4, and the specific enthalpy of the effluent gases is computed for the specified values of the parameters mentioned above. The gas mixture heat output is calculated as follows: W6=H6G1, kW, where T g H = ∫ C ⋅ dT 6 p 300 is the specific enthalpy of the gas mixture.

1, 2 is KBC gasification in air and steam medium and 3, 4 is CP gasification in air and steam medium correspondingly increases with the temperature in both variants of CP gasification, and reaches 100% at close and at relatively low values of temperature, which is 1,100 K. The SPCs for the gasification processes were calculated by the difference of working medium (solid fuel and oxidant) enthalpy at initial (T = 298 K) and final (current temperature of the process) conditions. The calculation results for both processes are presented in Figure 4.

2. 3. 4. 5. L. Wright, Coal Gasification – Back to the Future? – Perspective on Atmospheric vs Pressurized Coal Gasification (Proceedings of 28th International Technical Conference on Coal Utilization and Fuel systems, Clearwater, Florida, USA, Published by US Department of Energy & Coal Technology Association of USA, 2003 – CD p. 241–248). A. Ustimenko, F. Lockwood, E. Karpenko, V. Messerle, Plasma Complex Processing of Power Coals. (Proceeding of 6th International Conference on Technologies and Combustion for a Clean Environment “Clean Air”, Porto, Portugal, 2001, V.

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