METHOD AND INSTALLATION FOR PRODUCING depressant additives to diesel fuel, additives and DEPRESSONAYA DIESEL

摘要

1.method u043fu043eu043bu0443u0447u0435u043du0438u00a0 u0434u0435u043fu0440u0435u0441u0441u043eu0440u043du043eu0439 additive to diesel fuel by u0442u0435u0440u043cu043eu043eu043au0438u0441u043bu0438u0442u0435u043bu044cu043du043eu0439 reaction u0440u0430u0437u043bu043eu0436u0435u043du0438u00a0 u044du0442u0438u043bu0435u043du043fu0440u043eu043fu0438u043bu0435u043du043eu0432u043eu0433u043e copolymer comprising oxidation u044du0442u0438u043bu0435u043du043fu0440u043eu043fu0438u043bu0435u043du043eu0432u043eu0433u043e copolymer in a solvent in the presence of u043eu043au0438u0441u043bu0438u0442u0435u043bu00a0 served in the reaction environment in the oxidizing reaction of the heat re u0430u043au0446u0438u043eu043du043du043eu0439 environment, u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 orderwhat is used as a u044du0442u0438u043bu0435u043du043fu0440u043eu043fu0438u043bu0435u043du043eu0432u043eu0433u043e copolymer rubber with powdered synthetic u044du0442u0438u043bu0435u043du043fu0440u043eu043fu0438u043bu0435u043du043eu0432u044bu0439 u043cu043eu043bu0435u043au0443u043bu00a0u0440u043du043eu0439 mass 300000 - 1 million, as u0440u0430u0441u0442u0432u043e u0440u0438u0442u0435u043bu00a0 using hydrocarbon C10 - C18, u043eu0441u0443u0449u0435u0441u0442u0432u043bu00a0u044eu0442 u0442u0435u0440u043cu043eu043eu043au0438u0441u043bu0438u0442u0435u043bu044cu043du0443u044e reaction u0440u0430u0437u043bu043eu0436u0435u043du0438u00a0 at atmospheric pressure and temperature of the reaction environment $...210u0441 to u043eu0431u0440u0430u0437u043eu0432u0430u043du0438u00a0 reaction environment with the concentration of copolymer, not below 70%, the oxidation u043fu0440u043eu0432u043eu0434u00a0u0442 u043cu043eu043bu0435u043au0443u043bu00a0u0440u043du044bu043c oxygen, with the air u0431u0430u0440u0431u043eu0442u0438u0440u0443u044e t through the reaction environment, and to stabilize the u0430u043cu0438u043du0441u043eu0434u0435u0440u0436u0430u0449u0438u043c stabilizer.;2. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that the u0442u0435u0440u043cu043eu043eu043au0438u0441u043bu0438u0442u0435u043bu044cu043du0443u044e reaction u0440u0430u0437u043bu043eu0436u0435u043du0438u00a0 of synthetic rubber in the presence of a catalyst in u044du0442u0438u043bu0435u043du043fu0440u043eu043fu0438u043bu0435u043du043eu0432u043eu0433u043e u043eu0441u0443u0449u0435u0441u0442u0432u043bu00a0u044eu0442 a salt of metal with variable u0432u0430u043bu0435u043du0442u043du043eu0441u0442u044cu044e, administrated by heating the reaction environment of 0.09...0,1 mas.% of the total mass of rubber and u0440u0430u0441u0442u0432u043eu0440u0438u0442u0435u043bu00a0.;3. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that, as the stabilizer using diethanolamine or u043cu043eu043du043eu044du0442u0430u043du043eu043bu0430u043cu0438u043d or u043fu043eu043bu0438u044du0442u0438u043bu0435u043du043fu043eu043bu0438u0430u043cu0438u043d.;4. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 3, so that an additional or u0444u0442u0430u043bu0438u0435u0432u044bu0439 u0432u0432u043eu0434u00a0u0442 maleic anhydride.;5. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 2, so that the metal salt with the variable u0432u0430u043bu0435u043du0442u043du043eu0441u0442u044cu044e choose group: u0441u0442u0435u0430u0440u0430u0442 u0441u0442u0435u0430u0440u0430u0442 manganese or iron or u0441u0442u0435u0430u0440u0430u0442 u0432u0430u043du0430u0434u0438u00a0 or u0441u0442u0435u0430u0440u0430u0442 cobalt.;6. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that a u0440u0430u0441u0442u0432u043eu0440u0438u0442u0435u043bu00a0 use u0442u0435u0442u0440u0430u0434u0435u0446u0435u043d and / or fractions of paraffins u044114 17, and / or the fraction of olefins C10 - C18.;7. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that the use of synthetic epdm rubber with u043cu043eu043bu0435u043au0443u043bu00a0u0440u043du043eu0439 mass 300000 - 1 million, and the solvent in proportion to the next u043eu043cu043fu043eu043du0435u043du0442u043eu0432 mas.% solvent, rubber 34 - 40, 60 - 66.;8.installation of u0434u043bu00a0 u043fu043eu043bu0443u0447u0435u043du0438u00a0 u0434u0435u043fu0440u0435u0441u0441u043eu0440u043du043eu0439 additives u0441u043eu0434u0435u0440u0436u0430u0449u0430u00a0 reactor, an area input source products, and the u0434u043bu00a0 its heating, u043eu0442u043bu0438u0447u0430u044eu0449u0430u00a0u0441u00a0, supplementary case contains colloid mill, the entrance of which u0441u0432u00a0u0437u0430u043d entering the reactor, the colloid mill is equipped with closed circuit u0434u043bu00a0 u0446u0438u0440u043au0443u043bu00a0u0446u0438u0438 u0433u043eu043cu043eu0433u0435u043du0438u0437u0438u0440u0443u0435u043cu043eu0439 among you connected the entrance and the exit with u0433u043eu043cu043eu0433u0435u043du0438u0437u0430u0442u043eu0440u043eu043c,the reactor further includes a device u0434u043bu00a0 u0431u0430u0440u0431u043eu0442u0438u0440u043eu0432u0430u043du0438u00a0 air through the reaction environment.;9. install the p.8, u043eu0442u043bu0438u0447u0430u044eu0449u0430u00a0u0441u00a0, entrance u0433u043eu043cu043eu0433u0435u043du0438u0437u0430u0442u043eu0440u0430 u0441u0432u00a0u0437u0430u043d post reactor through the rough and fine filters in cleaning.;10. install the p.8, u043eu0442u043bu0438u0447u0430u044eu0449u0430u00a0u0441u00a0, the reactor contains a closed loop u0434u043bu00a0 u043eu0442u0434u0435u043bu0435u043du0438u00a0 water from the gaseous products of the reaction, which is connected with the entrance and exit area stu input source products in the reactor through the heat exchanger;11. install the p.8, u043eu0442u043bu0438u0447u0430u044eu0449u0430u00a0u0441u00a0, the reactor contains a closed loop u0434u043bu00a0 u0446u0438u0440u043au0443u043bu00a0u0446u0438u0438 reaction environment, connected the entrance and the exit with the reactor.;12. install the p.8, u043eu0442u043bu0438u0447u0430u044eu0449u0430u00a0u0441u00a0, colloid mill includes a closed loop u0434u043bu00a0 u043eu0442u0434u0435u043bu0435u043du0438u00a0 water from gaseous products homogenization, the united front and the u044bu0445u043eu0434u043eu043c with u0433u043eu043cu043eu0433u0435u043du0438u0437u0430u0442u043eu0440u043eu043c through the heat exchanger.;13. u0434u0435u043fu0440u0435u0441u0441u043eu0440u043du0430u00a0 list of gasoline additives for diesel fuel, u043fu043eu043bu0443u0447u0435u043du043du0430u00a0 under mode 1.;14. diesel fuel on the basis of the base diesel fuel containing u0434u0435u043fu0440u0435u0441u0441u043eu0440u043du0443u044e u043fu0440u0438u0441u0430u0434u043au0443, u043eu0442u043bu0438u0447u0430u044eu0449u0435u0435u0441u00a0 so that as the additive it contains u043fu0440u0438u0441u0430u0434u043au0443 on p.10 sufficient u0434u043bu00a0 u0443u0441u043eu0432u0435u0440u0448u0435u043du0441u0442u0432u043eu0432u0430u043du0438u00a0 temperature u0437u0430u043cu0435u0440u0437u0430u043du0438u00a0 and limit temperature u0444u0438u043bu044cu0442u0440u0443u0435u043cu043eu0441u0442u0438.