Streamlined body, streamlined body APPLICATION AND DEVICE FOR BURNING FUEL MIXTURE

摘要

1. u043eu0431u0442u0435u043au0430u0435u043cu043eu0435 body u0434u043bu00a0 u043fu0440u0438u043cu0435u043du0435u043du0438u00a0 mode u0441u0436u0438u0433u0430u043du0438u00a0 in which surge manufacturing units are in the reaction chamber (4) of the fuel mixture, and u043eu0431u0442u0435u043au0430u0435u043cu043eu0435 body (1). its main axis is located inside the chamber in the direction of flow, u043eu0442u043bu0438u0447u0430u044eu0449u0435u0435u0441u00a0, u0432u043du0435u0448u043du00a0u00a0 surface u043eu0431u0442u0435u043au0430u0435u043cu043eu0433u043e body (1) formed by the top 100 rhone (11) u043fu0440u043eu0444u0438u043bu00a0 wing (15) around its u0445u043eu0440u0434u044b (13).;2. on u043eu0442u043bu0438u0447u0430u044eu0449u0435u0435u0441u00a0 body 1, so that it is accomplished with the u0438u0437u043cu0435u043du00a0u0435u043cu043eu0439 geometries.;3. the application of u043eu0431u0442u0435u043au0430u0435u043cu043eu0433u043e body (1) on one of the u043fu043f.1 and 2 u0434u043bu00a0 u0441u043eu0437u0434u0430u043du0438u00a0 laminar flow.;4. the application of u043eu0431u0442u0435u043au0430u0435u043cu043eu0433u043e body (1) on one of the u043fu043f.1 and 2 by u043fu043eu043cu0435u0449u0435u043du0438u00a0 u043eu0431u0442u0435u043au0430u0435u043cu043eu0433u043e body (1) of the main axis in the direction of flow in the free flow of u0434u043bu00a0 usually caesarean u0441u043eu0437u0434u0430u043du0438u00a0 u043fu043eu0434u0441u0430u0441u044bu0432u0430u044eu0449u0435u0433u043e u0434u0435u0439u0441u0442u0432u0438u00a0 in the direction of flow.;5. the application of u043eu0431u0442u0435u043au0430u0435u043cu043eu0433u043e body (1) on one of the u043fu043f.1 and 2 as a heat exchanger by u043fu043eu043cu0435u0449u0435u043du0438u00a0 u0442u0435u043fu043bu043eu043fu0440u043eu0432u043eu0434u00a0u0449u0435u0433u043e u043eu0431u0442u0435u043au0430u0435u043cu043eu0433u043e body (1) in the flow of heat u0433u0440u0430u0434u0438u0435u043d tom.;6. the application of u043eu0431u0442u0435u043au0430u0435u043cu043eu0433u043e body (1) on one of the u043fu043f.1 and 2, in which u0437u0430u0434u043du00a0u00a0 u043au0440u0438u0442u0438u0447u0435u0441u043au0430u00a0 point (3) u043eu0431u0442u0435u043au0430u0435u043cu043eu0433u043e body (1) is located downstream.;7. the application of u043eu0431u0442u0435u043au0430u0435u043cu043eu0433u043e body (1) on one of the u043fu043f.1 and 2 or 6 as a surface u0441u0442u043eu043bu043au043du043eu0432u0435u043du0438u00a0 u0434u043bu00a0 incoming fuel mixture.;8. application on p.7 u0434u043bu00a0 separation and / or u0440u0430u0441u043fu0440u0435u0434u0435u043bu0435u043du0438u00a0, u0440u0430u0441u043fu044bu043bu0435u043du0438u00a0 or u0438u0437u043cu0435u043bu044cu0447u0435u043du0438u00a0 u0438u043cu0435u044eu0449u0438u0445u0441u00a0 in fuel mixture of gaseous, liquid and / or solid components.;9. application on p.7 or 8 u0434u043bu00a0 u0437u0430u043cu0435u0434u043bu0435u043du0438u00a0 components of fuel mixture, u0434u043bu00a0 u0443u0432u0435u043bu0438u0447u0435u043du0438u00a0 duration u043fu0440u0435u0431u044bu0432u0430u043du0438u00a0 these components and u0434u043bu00a0 more intensive u0441u043cu0435u0448u0438u0432u0430 u043du0438u00a0 these components.;10. the application of u043eu0431u0442u0435u043au0430u0435u043cu043eu0433u043e body (1) on one of the u043fu043f.1 and 2 or on one of the u043fu043f.6 - 9 u0434u043bu00a0 u0443u0441u043au043eu0440u0435u043du0438u00a0 flow of fuel mixtures and products in the reaction chamber u0441u0433u043eu0440u0430u043du0438u00a0 manufacturing units e (4) in the direction of graduation u043eu0442u0432u0435u0440u0441u0442u0438u00a0 this cell.;11. the application of u043eu0431u0442u0435u043au0430u0435u043cu043eu0433u043e body (1) on one of the u043fu043f.1 and 2 or on one of the u043fu043f.6 10 as a heat exchanger u0434u043bu00a0 heating fuel mixture.;12. the device u0434u043bu00a0 u0441u0436u0438u0433u0430u043du0438u00a0 fuel mixture, u0445u0430u0440u0430u043au0442u0435u0440u0438u0437u0443u044eu0449u0435u0435u0441u00a0 manufacturing units, that contains a reaction chamber (4) and is its main axis within the chamber the direction of the flow of u043eu0431u0442u0435u043au0430u0435u043cu043eu0435 body (1), which is formed by u0432u043du0435u0448u043du00a0u00a0 surface upper part (11) u043fu0440u043eu0444u0438u043bu00a0 wing (15) around its u0445u043eu0440u0434u044b (13).;13. device for u0445u0430u0440u0430u043au0442u0435u0440u0438u0437u0443u044eu0449u0435u0435u0441u00a0 p.12, so that manufacturing units u0440u0435u0430u043au0446u0438u043eu043du043du0430u00a0 chamber (4) has a lower section (5) of cylindrical shape, which is adjacent to u043au043eu043du0443u0441u043eu043eu0431u0440u0430u0437u043du043e u0443u0436u0430u044eu0449u0438u0439u0441u00a0 station (6), which is adjacent to the head (7) form with high u0440u0430u0441u0448u0438u0440u00a0u044eu0449u0438u043cu0441u00a0 section, u0437u0430u043au0430u043du0447u0438u0432u0430u044eu0449u0430u00a0u0441u00a0 graduation hole (8).;14. device for u0445u0430u0440u0430u043au0442u0435u0440u0438u0437u0443u044eu0449u0435u0435u0441u00a0 p.13, so that u043eu0431u0442u0435u043au0430u0435u043cu043eu0435 body (1) of its main axis is located on the central axis of the reaction chamber manufacturing units (4), in particular with agriculture u043eu0436u043du043eu0441u0442u044cu044e u0441u043cu0435u0449u0435u043du0438u00a0.