By Nick Syred, Artem Khalatov

The NATO ARW complex Combustion and Aerothermal applied sciences: Environmental defense and pollutants rate reductions, used to be held in Kiev, might 2006. The workshop was once Co-Directed via Profs. N. Syred and A.Khalatov, winners of the NATO clinical Prize 2002, and used to be equipped via the Institute of Thermophysics (Ukraine) and Cardiff college, united kingdom. the first Workshop goals have been to evaluate the present wisdom on complex combustion and aerothermal applied sciences delivering diminished environmental influence, to spot instructions for destiny learn within the box, and to advertise the shut relationships and enterprise contacts among scientists from NATO and companion international locations.

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The special combined plasma chemical reactor (CPCR) for coal gasification allows the processes for the thermoimpact on solid fuel to be performed to obtain synthesis gas free from nitrogen and sulfur oxides. 5–15 kg/h. High quality syngas was produced from the both solid fuels. PLASMA GASIFICATION 143 2. Numerical Simulation The software Code TERRA4 was used for the thermodynamic analysis of the solid fuels plasma gasification process. This software was created for equilibrium computations of high-temperature processes, and in contrast to traditional thermochemical methods of equilibrium computation that use the Gibbs energy, equilibrium constants and Guldberg and Vaage law of acting mass, TERRA is based on the principle of maximizing entropy for isolated thermodynamic systems in equilibrium.

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. III, pp. 1473–1480). Jieshan Qiu, Xiaojun He, Tianjun Sun, Zongbin Zhao, Ying Zhou, Shuhong Guo, Jialiang Zhang, Tengcai Ma, Coal gasification in steam and air medium under plasma conditions: a preliminary study, Fuel Processing Technology, (85), 969–982 (2004). M. I. C. E. G. B. Ustimenko, Plasma technologies for solid fuels: experiment and theory, Journal of the Energy Institute, 78(4), 157–171 (2005).

CP 6. 1 kWh/kg of syngas. 3%. 4 kg/h, the mass-averaged temperatures in the reactor increases from 2,100 to 2,850 K and the corresponding intensification of the process. 2%. 3%). Note that contrary to the gasification under air-plasma conditions, for the process of plasma gasification in steam medium the concentration of hydrogen in the syngas is higher than the concentration of carbon dioxide. The hydrogen concentration produced for the gasification in steam is 3–4 times higher than that produced in the air medium.

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